WO2007146922A2 - Fibrous materials and compositions - Google Patents

Fibrous materials and compositions Download PDF

Info

Publication number
WO2007146922A2
WO2007146922A2 PCT/US2007/070972 US2007070972W WO2007146922A2 WO 2007146922 A2 WO2007146922 A2 WO 2007146922A2 US 2007070972 W US2007070972 W US 2007070972W WO 2007146922 A2 WO2007146922 A2 WO 2007146922A2
Authority
WO
WIPO (PCT)
Prior art keywords
fibrous material
fibrous
acid
inch
percent
Prior art date
Application number
PCT/US2007/070972
Other languages
French (fr)
Other versions
WO2007146922A3 (en
Inventor
Marshall Medoff
Original Assignee
Xyleco, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to EA200970015A priority Critical patent/EA013498B1/en
Priority to MX2012012922A priority patent/MX342620B/en
Priority to EP16189685.7A priority patent/EP3135379B1/en
Priority to DK07798424.3T priority patent/DK2032261T3/en
Priority to KR1020097000485A priority patent/KR101159628B1/en
Priority to BRPI0713417-7A priority patent/BRPI0713417B1/en
Priority to CA2655111A priority patent/CA2655111C/en
Priority to EP07798424.3A priority patent/EP2032261B1/en
Priority to PL07798424T priority patent/PL2032261T3/en
Priority to SI200731733A priority patent/SI2032261T1/en
Priority to AP2008004725A priority patent/AP2464A/en
Priority to BR122017001646A priority patent/BR122017001646B1/en
Priority to MX2008016029A priority patent/MX2008016029A/en
Priority to AU2007257741A priority patent/AU2007257741B2/en
Application filed by Xyleco, Inc. filed Critical Xyleco, Inc.
Priority to ES07798424.3T priority patent/ES2558308T3/en
Priority to PL16189685T priority patent/PL3135379T3/en
Priority to EP18213457.7A priority patent/EP3492173A3/en
Priority to BR122018075069-3A priority patent/BR122018075069B1/en
Publication of WO2007146922A2 publication Critical patent/WO2007146922A2/en
Priority to IL195910A priority patent/IL195910A/en
Publication of WO2007146922A3 publication Critical patent/WO2007146922A3/en
Priority to IL228130A priority patent/IL228130A/en
Priority to IL228131A priority patent/IL228131A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/0026Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
    • B29B17/0042Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting for shaping parts, e.g. multilayered parts with at least one layer containing regenerated plastic
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/08Conditioning or physical treatment of the material to be shaped by using wave energy or particle radiation
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/08Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/08Radiation
    • A61L2/081Gamma radiation
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/08Radiation
    • A61L2/082X-rays
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/08Radiation
    • A61L2/087Particle radiation, e.g. electron-beam, alpha or beta radiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C19/00Other disintegrating devices or methods
    • B02C19/0056Other disintegrating devices or methods specially adapted for specific materials not otherwise provided for
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • B02C23/08Separating or sorting of material, associated with crushing or disintegrating
    • B02C23/10Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • B02C23/08Separating or sorting of material, associated with crushing or disintegrating
    • B02C23/14Separating or sorting of material, associated with crushing or disintegrating with more than one separator
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B17/0412Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/08Making granules by agglomerating smaller particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C43/00Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
    • B29C43/003Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C43/00Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
    • B29C43/02Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/0001Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/0005Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor using fibre reinforcements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/24Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 characterised by the choice of material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L97/00Compositions of lignin-containing materials
    • C08L97/02Lignocellulosic material, e.g. wood, straw or bagasse
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/02Monosaccharides
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/14Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/08Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
    • C12P7/10Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing cellulosic material
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/16Butanols
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0217Mechanical separating techniques; devices therefor
    • B29B2017/0224Screens, sieves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B2017/0424Specific disintegrating techniques; devices therefor
    • B29B2017/0476Cutting or tearing members, e.g. spiked or toothed cylinders or intermeshing rollers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0029Perfuming, odour masking or flavouring agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0032Pigments, colouring agents or opacifiyng agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • B29K2105/065Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts containing impurities
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • B29K2105/12Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of short lengths, e.g. chopped filaments, staple fibres or bristles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • B29K2105/16Fillers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/25Solid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2201/00Use of cellulose, modified cellulose or cellulose derivatives, e.g. viscose, as reinforcement
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037Other properties
    • B29K2995/0059Degradable
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P2203/00Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/49801Shaping fiber or fibered material

Definitions

  • This invention relates to fibrous materials and to compositions.
  • Fibrous materials e.g., ceHuIosic arid IignoccHuiosic materials, are produced, processed, and used in large quantities in a number of applications. Often such fibrous materials are ust- ⁇ once, and then discarded as waste.
  • this invention relates to fibrous materials, methods of making fibrous materials, compositions that include fibrous materials (e.g.. composites that include the fibrous materials and a resin, or compositions that include the fibrous materials and bacteria and/or an enzyme), and to uses of the same.
  • the compositions car: be used to make ethauoi, or a by-product, such as a protein or ligrmi, or applied to a structure as insulation.
  • any of the fibrous materials disclosed herein can be used in combination with, any of the fibrous materials, resins, additives, or other components disclosed in U.S. Patent Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105. Tn turn, these fibrous materials and/or components can be used in any of the applications, products, procedures, et cetera disclosed in any of these patents or in this application.
  • the fibrous materials or compositions thai include the fibrous materials can be, e.g., associated with, blended with, adjacent to, surrounded by, or within a structure or carrier (eg., a netting, a membrane, a flotation device, a bag, a shell, or a biodegradable substance).
  • a structure or carrier eg., a netting, a membrane, a flotation device, a bag, a shell, or a biodegradable substance.
  • the structure or carrier may itself be made from a fibrous materia!, or of a composition that includes a fibrous material,
  • the fibrous material is combined wi ⁇ i a material, such as a protic acid, that enhances the rate of biodegradatio ⁇ of the fibrous material
  • the fibrous materia! is combined with a material that retards degradation of the fibrous material, such as a buffer.
  • the ratio of fibrous materials to the other components of the compositions will depend upon the nature of the components, and can be readily adjusted for a specific product application.
  • any of the fibrous materials described herein can be used, e.g., to form composites with resin, or can be combined with bacteria and/or one or more enzymes to produce a valuable product, such as a fuel (e.g., etha ⁇ oL a hydrocarbon, or hydrogen).
  • a fuel e.g., etha ⁇ oL a hydrocarbon, or hydrogen.
  • the invention features methods of making fibrous materials.
  • the methods include shearing & fiber source to provide a first fibrous material, and passing the first fibrous material through a Clear screen having an average opening size of 1.59 mm or less ( L' 16 inch. 0.0625 inch) to provide a second fibrous material.
  • the fiber .source can, e.g., be cut into pieces or strips of confetti-like material prior to the shearing.
  • the average opening size of the first screen is less than 0.79 mm (1/32 inch, 0.03125 inch), e.g., less than 0.40 mm ( 1/64 inch, 0.015625 inch), less fa 0.20 ram (1/128 inch, 0.007S 125 inch), or even less than 0.10 mm (1/256 inch, 0.00390625 inch ⁇ , hi specific implementations, the shearing is performed with a rotary knife cutter. If desired, the shearing can be performed while the fiber source is dry (e.g., having leas than 0.25 percent by weight absorbed water), hydrated, or even while the fiber source is partially or fully submerged in a liquid, such as water or isopropariol.
  • the second fibrous material can, e.g., be collected in a bin having a pressure below nominal atmospheric pressure, e.g., at least H) percent below nominal atmospheric pressure, at least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure.
  • the second fibrous material can, e.g., be sheared once or numerous times, e.g., twice, thrice, or even more, e.g., ten times. Shearing can "open up" and/or "stress" the fibrous materials, making the materials more disperssbie, e.g., in a solution or in a resin.
  • the second fibrous material can be, e.g., sheared and the resulting fibrous material passed through the iirsi screen.
  • the second fibrous material can be sheared, and the resulting fibrous material passed through a second screen having an average opening size less than the first screen, providing a third fibrous material
  • a ratio of an average length-to-diameter ratio of the second fibrous material to an average fength-io-diameter ratio of the third fibrous materia! ears be, e.g., less than 1.5, less than i .4, less than 1.25, or even less thai 1.1.
  • the second fibrous can be, e.g., passed through a second screen having an average opening size less than the first screen.
  • the shearing and passing can be, e.g., performed concurrently.
  • the second fibrous material can have an average Jengih-to-diameter ratio of, e.g.. greater than H)Zi , greater than 25/ i , or even greater than 50/1.
  • an average length of the second fibrous material can be between 0,5 mm and 2.5 ram, e.g., between 0.75 mm and LO mm.
  • an average width of the second fibrous material can be between 5 ⁇ m and 50 ⁇ rrs, e.g., between 10 ⁇ m and 30 ⁇ m,
  • a Standard deviation of a length of the second fibrous material can be less than 60 percent of an average length of the second fibrous material, e.g., less than. 50 percent of an average length of the second fibrous materia!.
  • a BBT surface area of the second fibrous material is greater t ' heart 0.5 nr/g, e.g., greater than l . ⁇ ⁇ r/g, greater than 1.5 m ' 7g, greater than 1,75 ⁇ ; / g, greater than 2,5 rrr/g, greater than 10.0 mVg, greater than 25.0 Tn-Vg, greater than 50.0 nr/g, or even greater than 100.0 m7g.
  • a porosity of the second fibrous material is greater than 25 percent, e.g., greater than 50 percent, greater than 75 percent, greater than SS percent, greater than 90 percent, greater than 92 percent, greater than 95 percent, or even greater than 99 percent.
  • the screen is formed by interweaving monofilaments.
  • the fiber source cars include, e.g., a ecHulosie material a lignoee ⁇ ulosk material.
  • the liber source includes a blend of fibers, e.g., fibers derived from a paper source and fibers derived from a textile source, e.g., cotton.
  • the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; and passing the fibrous materia! through a first screen to provide a second fibrous materia!.
  • a ratio of an average leng ⁇ i-to-diametcr ratio of the first fibrous material to an average length-to-diamcter of the second fibrous material is less than 1.5.
  • the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; passing the fibrous material through a first screen to provide a second fibrous material; and then shearing the second fibrous material again to provide a third fibrous materia],
  • the invention features composites or compositions made from any of the fibrous materials described herein.
  • compositions can include any of the fibrous materials described herein and a bacterium and/or an enzyme.
  • the compositions thai include any of the fibrous materials described herein and die bacterium and/or enzyme can be in. a dry state, or they can include a liquid, such as water.
  • the composite can be in the form of a stepping stool, pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, iool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings., above- axsd below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, bangers, servers, caskets, book covers, canes and cratches.
  • the invention features fibrous materials having an average length- to-diamet ⁇ r ratio of greater than 5, and having a standard deviation of a fiber length of less than sixty percent of an average fiber length.
  • the average le ⁇ gth-to ⁇ diameter ratio can be greater than 10/1 , e.g., greater than 15/1 , greater than 25/1 , greater than 35/1 , greater than 45/1 , or even greater than 50/1.
  • she average length can be between 0.5 mm and 2,5 mm.
  • the invention features methods of making fibrous materials that include shearing a liber source to provide a first fibrous material; collecting the first fibrous material; and then shearing the first fibrous to provide a second fibrous material
  • the invention features methods of making a useful material, such as a fuel.
  • the methods include shearing a fiber source to provide a First fibrous material; passing the first fibrous materia! through a first screen having an average opening size of about 1.59 mm or less (1/16 inch, 0,0625 inch) to provide a second fibrous materia!; and combining the second fibrous material with a bacterium and/or enzyme > the bacterium and/or enzyme utilizing the second fibrous material to produce a fuel that includes hydrogen, an alcohol, an organic acid and/or a hydrocarbon
  • the alcohol can be, e.g., methanol, ethanoL propanoic isopropa ⁇ oL butanol, ethylene glycol, propylene glycol, 1, 4-hutane dial, glycerin, or mixtures of these alcohols;
  • the organic acid can be, e.g., malomc acid, succinic acid, glutaric acid, oleic acid, liriolek acid,
  • any of the fibrous materials described herein can be hydrolyzed to break down higher molecular weight carbohydrates ink) lower molecular weight carbohydrates.
  • the invention features methods of making a useful material, such as a fuel, by shearing a, liber source or a fibrous material, and then combining if with a bacterium and/or an enzyme.
  • a useful material such as a fuel
  • the fiber source can be sheared once to provide a fibrous material, arid then the fibrous material can be combined with a bacterium and/or an eiixyrne to make the useful material.
  • the invention features methods of de ⁇ s ⁇ fying fibrous compositions.
  • the methods include shearing a fiber source to provide a fibrous material; combining the fibrous material with a bacterium and/or enzyme to provide a fibrous material composition: encapsulating the composition in a substantially gas impermeable materia!; find removing entrapped gas from the encapsulated composition to densify the composition.
  • the gas impermeable material can be in the form of a bag, and. the composition can be deasified by evacuating air from the bag, and then sealing the bag.
  • the invention features composites that include s fibrous material, a resin and a dye.
  • the fibrous material can have an average lengih-to-diaincter ratio of greater than 5, and a standard deviation of a liber length of less than sixty percent of an average fiber length,
  • the composite additionally includes a pigment, ⁇ n some implementations, the dye soaked into or surfaced on the fibers.
  • the invention features methods of making composites that include dyeing a fibrous material; combining the fibrous material with a resin; and forming a composite from the combination,
  • the invention features methods of making composite ihat include adding a dye to a resin to provide a dye/resin combination; combining the dye/resin combination with a fibrous material; and forming a composite from the dye/resin combination and fibrous material
  • Ebrous material is a material thai includes numerous loose, discrete and separable fibers.
  • a fibrous material can be prepared from a polycoated paper or a bleached Kraft paper fiber source by shearing, e.g., with a rotary knife cutter.
  • the term "screen”, as used herein, means a member capable of sieving material according to size, e.g., a perforated plate, cylinder or the like, or a wire mesh or cloth fabric.
  • Embodiments and/or aspects can have any one of, or combinations of, the following advantages.
  • the fibrous materials axe opened up and/or stressed, making the materials more dispcrsible, e.g., in a solution or in a resin, and making them more susceptible to chemical, enzymatic or biological attack.
  • the fibrous materials can have, e.g., a relatively narrow length and/or iength-to-diameter ratio distribution, such that their properties are consistently defined.
  • the fibers of the fibrous materials when blended with a molten resin or a solution, can modify the rheology of the molten resin, or solution in a consistent and predieable manner, e.g., resulting in resin/fibrous material combinations that are, e.g., easier to mold and extrude.
  • the fibrous materials can easily pass through small openings or channels, such as those found in or associated with injection molds, e.g., gates or hot runners. Paris molded from such fibrous materials can exhibit a good surface finish, e.g., with few visible speckles of large particles and/or agglomerated particles,
  • Fig. 1 is block diagram illustrating conversion of a fiber source into a first and second fibrous material.
  • Fig, 2 is a cross-sectional view of a rotary knife cutter, figs. 3-8 are top views of a variety of screens made from monofilaments.
  • Fig. 9 is block diagram illustrating conversion of a fiber source into a first, second and third fibrous material.
  • Figs. 1OA arid 1OB are photographs of fiber sources; Fig, iOA being a photograph of a polyeoated paper container, and Fig, 1 OB being a photograph of unbleached Kraft paper rolls.
  • FIG. -1 as. ! and 12 are scanning electron micrographs of a fibrous materia! produced from polycoa .ed paper at 25 X magnification and 1000 X magnification, respectively.
  • the fibrous mater! al was produced on a rotary knife cutter utilizing a screen with i /S inch openings.
  • Figs. 13 ar ⁇ l 14 are scanning electron micrographs of a fibrous material produced from bleached Kraft, board paper at 25 X magnification and IC 1 OO X magnification, respectively.
  • the iibr ⁇ i-s material was produced on a rotary knife cutter utilizing a screen with 1/8 inch openings.
  • Figs. 15 and 16 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 X magnification and ! 0OO X magnification, respectively. The fibrous material was twice sheared on a rotary knife cutter utilizing a screen with l/ ' i ⁇ inch openings during each shearing.
  • Figs, 17 and 18 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 X magnification and 1 OCl(J X magnification, respectively. The fibrous material was thrice sheared on a rotary knife c utter.
  • fig. 19 is a block diagram illustrating revertible bulk densifieaiion of a fibrous materia! composition.
  • a fiber source 10 is sheared, e.g., in a rotary knife cutter, to provide a iirsi fibrous materia] 12.
  • the first fibrous material 12 is passed through a first screen 16 having an average opening size of 1 ,59 mm or less (1 /16 inch, 0.0625 inch) to provide a second fibrous material .14, if desired, fiber source 10 can be cut prior to the shearing, e.g , with a shredder.
  • the paper when a paper is used as the fiber source the paper can be first cut into strips that are, e.g., 1/4- to 1/2-inch wide, using a shredder, e.g., a counter-rotating screw shredder, such as those manufactured by Munson (Utica, N. Y.).
  • a shredder e.g., a counter-rotating screw shredder, such as those manufactured by Munson (Utica, N. Y.
  • the paper can be reduced in size by catting to a desired size using a guillotine cutter.
  • the guillotine cotter cars be used to cut the paper irsio sheets that are, e.g., 10 inches wide by 12 inches long.
  • the shearing of fiber source 10 and the passing of the resulting first tibrous material 12 through first screen 16 are performed concurrently.
  • the shearing and the passing can also be performed in a batch-type process.
  • a rotary knife carter can he used to concurrently shear the fiber source 1 (I and screen the first fibrous materia! 12,
  • a rotary knife cutter 20 includes a hopper 22 that can be loaded with a shredded fiber source H)" prepared by shredding i ⁇ bcr source 10.
  • Shredded fiber source i 0' is sheared between stationary blades 24 and rotating blades 26 to provide a first fibrous material 12
  • First fibrous material 12 passes through screen 16 having the dimensions described above, and the resulting second fibrous material 14 is captured in bin 30.
  • bin 30 can have a pressure below nominal atmospheric pressure, e.g., at least 10 percent below nominal atmospheric pressure, e.g., at least 25 percent below nominal atmospheric pressure, ni least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure,
  • a vacuum source 50 (Fig, 2) is utilized to maintain the bin below nominal atmospheric pressure.
  • Shearing can be advantageous for "opening up” and “stressing" the fibrous materials, making the materials more dispersible, e.g., in a solution or in a resin, and making them more susceptible to chemical, enzymatic or biologies! attack.
  • shearing can iiinciionalize fiber surfaces with functional groups, such as hydroxy! or carboxylic acid groups, which can, e.g., help disperse the fibers in a molten resin or enhance chemical or biological attack.
  • the fiber source can be sheared in a dry state, a liydrated state (e.g., having up to ten percent by weight absorbed water), or in a wet state, e.g., having between about i 0 percent and about 75 percent by weight, water.
  • the fiber source can even be sheared while partial iy or fully submerged under a iiqnid, such as water, efhanoL isopropanol.
  • the fiber source can also be sheared in under a gas (such as a stream or atmosphere of gas other than air), e.g., oxygen or nitrogen, or steam.
  • a gas such as a stream or atmosphere of gas other than air
  • Other methods of making the fibrous materials include stone grinding, mechanical ripping or tearing, pin grinding or air attrition nulling.
  • the fibrous materials can be separated, e.g., continuously or in batches, into fractions according to their length, width, density, material type, or some combination of these attributes. For example, for forming composites, it is often desirable to have a relatively narrow distribution of fiber lengths. In addition, e.g., when making compositions that include bacteria and/or an enzyme, it is often desirable to use a substantially single material as a feedstock.
  • ferrous materials can be separated from any of the fibrous materials by passing a fibrous material that includes a ferrous materia] past a magnet, e.g., an electromagnet, and then passing the resulting fibrous material through a series of screens, each screen having different sized apertures.
  • a magnet e.g., an electromagnet
  • the fibrous materials can also be separated, e.g., by using a high velocity gas, e.g., air. in such an approach, the fibrous materials are separated by drawing off different fractions, which can be characterized photonic-ally, if desired.
  • a high velocity gas e.g., air.
  • Such a separation apparatus is discussed in Lindsey et a!, U.S. Patent No. 6,883,667, the entire disclosure of which is hereby incorporated by reference herein in its entirety.
  • the fibrous materials can be used immediately following their preparation, or they can may be dried, e.g.. at approximately 105 °C for 4-18 hours, so that the moisture content is, e.g., less than about 0.5% before use.
  • lignin can be removed from any of the fibrous materials that include H gain, such as Hgnoedlulosie materials.
  • the fibrous material can be sterilized Io kill any microorganisms that may be on the fibrous material.
  • the fibrous material can be sterilised by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation.
  • the 'fibrous materials can also be sterilized by temperature adjustment, e.g., heating or cooling fee fibrous material under conditions and for a sufficient time to kill any microorganisms, or by employing a chemical sterilant, such as bleach (e.g., sodium hypochlorite), ehlorhexidine, or ethylene oxide.
  • a chemical sterilant such as bleach (e.g., sodium hypochlorite), ehlorhexidine, or ethylene oxide.
  • the fibrous materials can also be sterilized by using a competitive organism, such as yeast against bacteria.
  • the average opening S ⁇ KC of the first screen 16 is less than 0.79 mm (1/32 inch, 0.03125 inch), e.g., less than (3.51 mm (1/50 inch, 0,02000 inch), less than 0.40 r ⁇ m (1/64 inch, 0,01 S625 inch), less than 0.23 mm (0.009 inch), less than 0.20 ram (1/128 inch, 0,0078125 inch). less than O.I S mm (0.007 inch), less than 0.13 mm (0,005 inch), or even less than less than 0.10 mm (1/256 inch, 0.00390625 inch).
  • Screen 16 is prepared by interweaving monofilaments 52 having an appropriate diameter to give the desired opening size.
  • the monofilaments can he made of a metal, e.g., .stainless steel. As the opening sizes get smaller, structural demands o.n the monofilaments may become greater. For example, for opening sizes less than 0.40 mm, it can !> ⁇ advantageous to make the screens from .monofilaments made from a material other than stainless steel, e.g.. titanium, titanium alloys, amorphous metals, nickel tungsten, rhodium, rhenium, ceramics, or glass.
  • the screen is made ⁇ mm a plate, e.g. a metal plats, having apertures, e.g., cut into the plate using a laser.
  • the second fibrous 14 is sheared and passed through the first screen 16, or a different sized screen, In some embodiments, the second fibrous material 14 is passed through a second screen having an average opening size equal to or less than that of first screen HS.
  • a third fibrous material 62 can be prepared from the second fibrous materia] 14 by shearing the second fibrous material 14 and passing the resulting materia! through a second screen 60 having an average opening sixe ! ⁇ ss than the first screen 16.
  • Fiber sources include eelkdosie liber sources, incmding paper and paper products like those shown in Figs. ISA (polye retardd paper) and 1OB (Kraft paper), and iig ⁇ ocellulosic liber sources, including wood, and wood-related materials, e.g., particle board.
  • Fiber sources include natural fiber sources, e.g., grasses, rice hulls, bagasse, co.to ⁇ , jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, rice bulls, coconut hair; fiber sources high in ⁇ -ceJluiose content, e.g., cotton; synthetic fiber sources, e.g., extruded yam (oriented yam or usi-oriented yam) or carbon fiber sources; inorganic fiber sources; and metal fiber sources. Natural or synthetic fiber sources can be obtained from virgin scrap textile materials, e.g., remnants or they can be post consumer waste, e.g., rags.
  • natural fiber sources e.g., grasses, rice hulls, bagasse, co.to ⁇ , jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, rice bulls, coconut hair
  • fiber sources high in ⁇ -ceJluiose content e.
  • paper products When paper products are used as fiber sources, they can be virgin materials, e.g., scrap virgin materials, or they can be past-consumer waste. Aside from virgin raw materials, post-consumer, industrial (e.g., offal), and processing waste (e.g., effluent from paper processing) can also be used as fiber sources. Also, the fiber source can be obtained or derived from human (e.g., sewage), animal or plant wastes. Additional fiber sources have been described in U.S. Patent Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 aid 5,952,105, each of which is incorporated by reference herein in its entirety.
  • Blends of any of the above fibrous sources may be used.
  • the fibers of the fibrous materials can have a relatively large average length-to-diameier ratio (e.g., greater than 2(Ro-I), even if they liavt- been sheared more lhayj once.
  • the fibers of the fibrous materials described herein may have a relatively narrow length and/or length-to-diameter ratio distribution.
  • the relatively large average fength-to-diameter ratio and the relatively narrow length and/or length -to-diameter ratio distribution are, at least in part, responsible for the ease at which the fibrous materials are dispersed in a resin, e.g., a molten thermoplastic resin.
  • the relatively large average length-to-diameter ratio and the relatively narrow length and/or ie ⁇ glh-to- dia ⁇ mei ⁇ r ratio distribution are, at least in part, responsible for the consistent properties of the fibrous materials, the predictable rheoiogy modification the fibrous materials impart on a resin, the ease at which the combinations of the fibrous materials and resins are east, extruded and injection molded, the ease in which the fibrous materials pass through small, often torturous channels and openings, and the excellent surface finishes possible with molded parts, e.g., glossy finishes and/or finishes substantially devoid of visible speckles.
  • average fiber widths are those determined optically by randomly selecting approximately 5,000 fibers.
  • Average liber lengths are corrected length-weighted lengths, BET (Bmnauer, Emmet and Teller) surface areas are multi-point surface areas, arid porosities are those determined by mercury poros ⁇ netry.
  • the average length-to-diameler ratio of the second fibrous material 14 can be, e.g. greater than 8/1, e.g,, greater than 10/1, greater than 15/1, greater than 20/1, greater than 25/1, or greater than 50/ J .
  • An average length of the second fibrous material 14 can be, e.g., between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 mm, and an average width (i.e., diameter) of the second fibrous material 14 can be, e.g.. between about 5 ⁇ m and 50 ⁇ m f e.g., between about K) ⁇ m and 30 ⁇ m.
  • a standard deviation of the length of the second fibrous material 14 is less than 60 percent of an average length of the second fibrous material 14, e.g., less than 50 percent of the average length, less than 40 percent of the average length, less than 25 percent of the average length, less than 10 percent of the average length, less th&n 5 percent of the average length, or even less than 1 percent of the average length.
  • a BET surface area of the second fibrous materia! 14 is greater than.
  • O.I m7g e.g., greater than 0.25 rr ⁇ 'g, greater than 0.5 m 2 /g, greater than 1.0 nr/g, greater than 1.5 m'/g, greater than 1.75 rr ⁇ ' g, greater than 5.0 ⁇ r/g, greater than 10 mv ' g, greater than 25 m"/g, greater than 35 nr/g, greater than 50.rrf /g, greater than 60 rrr/g, greater than 75 ⁇ r/g, greater than 100 m ' Vg, greater than 150 ⁇ r/g, greater than 200 nr/g, or even greater than 250 nr/g.
  • a porosity of the second fibrous material 14 can be, e.g., greater than 20 percent, greater than.25 percent, greater than 35 percent, greater than 50 percent, greater than 60 percent, greater than 70 percent, e.g., greater than 80 percent, greater than. 85 percent, greater than 90 percent, greater than 92 percent, greater than 94 percent, greater than SKS percent, greater than 97,5 percent, greater than 99 percent; or even greater than 99.5 percent.
  • a ratio of the average le ⁇ gth-to- diameter ratio of the first fibrous material 12 to the average lengtb-to-diaraeter ratio of the second ribrous material 14 is, e.g., less than ! .S, e.g., less than 1.4, less than 1.25, less than U, less than ! .075, less than 1.05, less than 1.025, or even substantially equal to L
  • the second fibrous material 14 is sheared again and the resulting fibrous materia! passed through a second screen having an average opening size less than the first screen to provide a third fibrous material 62.
  • a ratio of the average length-to-diameter ratio of the second fibrous material 14 to the average length- to-diameier ratio of the third fibrous material 62 can be, e.g., less than 1.5, e.g., less than 1 ,4, less than 1.25, or even less than 1.1.
  • the- third fibrous material 62 is passed through a ihirtl screen to produce a fourth fibrous material.
  • ' Hie fourth fibrous material can be, e.g., passed through a fourth screen to produce a fifth material Similar screening processes can be repeated as many times as desired to produce the desired fibrous material having the desired properties.
  • the desired fibrous material includes fibers having art average lersgth-to-di&meter ratio of greater than 5 and having a standard deviation of the fiber length that is less than sixty percent of the average length.
  • the average length-to- diameter ratio can be greater than 10/ 1 , e.g., greater than 25/1 , or greater than 50/ 1
  • the average length can be between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 roxn.
  • An average width of the fibrous material can be between about 5 ⁇ ro and 50 ⁇ re, e.g.. between about 10 ⁇ m and 30 ⁇ m.
  • the standard deviation can be less than 50 percent of the average length, e.g., less than 40 percent, less than 30 percent, less than 25 percent, less than 20 percent, less than 10 percent, less than 5 percent, or even less than 1 percent of the average length.
  • a desirable fibrous material can have, e.g., a BET surface area of greater than 0.5 rrf/g, e.g., greater than 1.O nYVg, greater than 1.5 ⁇ 7g, greater th&n 1.75 rn/Vg., greater than 5 m 2 /g, greater than 10 m " 7g, greater than 25.0 rrr/g, greater than 50,0 rrr/g, greater than 75.0 nr/g, or even greater than 100.0 m " /g.
  • a desired material can have, e.g., a porosity of greater than 70 percent, e.g., greater than 80 percent, greater than 87.5 percent, greater than 90 percent, greater than 92.5, greater than 95, greater than 97.5, or even greater than 99 percent.
  • a particularly preferred embodiment has a BET surface area of greater than 1.25 rrf/g and a porosity of greater than 85 percent.
  • Composites including any of the fibrous materials or blends of any of the fibrous materials described herein including any of the fibrous materials disclosed in Ii, S. Patent Nos, 6,448,307, 6,258.876, 6,207,729, 5,973,035 and 5,952,105), e.g., the first 12 or second fibrous materia! 14, and a resin, e.g., a thermoplastic resin or a thermosetting resin, ears be prepared by combining the desired fibrous materia! and the desired resin.
  • the desired fibrous material can he combined with the desired resin, e.g., by mixing the fibrous material and the resin in an. extruder or other mixer, Ib form the composite, the fibrous material can be combined with the resin as the " fibrous materia!
  • thermoplastic resins inciude rigid and elasSomeric thermoplastics.
  • Rigid thermoplastics include polyolefins (e.g., polyethylene, polypropylene, or polyolefni copolymers), polyesters (e.g., polyethylene terephthakte), poiyamidcs (e.g., nylon 6, 6/12 or 6/10), and polyethyieneirnines.
  • ekstomerie thermoplastic resins include elastor ⁇ eric siyreme copolymers (e.g...
  • styrene-ethyiene-butyle ⁇ e-styrene copolymers p ⁇ lya ⁇ ride elastomers (e.g., poiyether-polyamide copolymers) and ethyl ⁇ ne-vinyl acetaie copolymer.
  • the thermoplastic resin has a melt Sow rate of between IO g/10 minutes to ⁇ ' O g/10 minutes, e.g., between 20 g/10 minutes to 50 g/10 minutes, or between 30 g/30 min ⁇ tes to 45 g/10 minutes, as measured ⁇ si ⁇ g ASTM 123 S.
  • compatible blends of any of the above thermoplastic resins cars be used,
  • the thermoplastic resin has a polydispersiiy index (PDf), i.e., a ratio of the weight average molecular weight to the number average molecular weight, of greater thim 1.5, e.g., greater than 2.0, greater than 2.5, greater than 5,0. greater than 7.5, or even greater than .10.0. in specific embodiments, polyoiefi ⁇ s or blends of pol yolefms are utilized as the thermoplastic resin.
  • PDf polydispersiiy index
  • thermosetting resins examples include natural rubber, butadiene-rubber and polyurethanes.
  • additives e.g., in the form of a solid or a liquid
  • suitable additives include fillers such as calcium carbonate, graphite, wollastonite, mica, glass, fiber glass, silica, and tale; inorganic flame retardants such as alumina irihydrate or magnesium hydroxide; organic flame rctardants such as chlorinated or brominat ⁇ d organic compounds; ground construction waste; ground tire rubber; carbon fibers; or metal fibers or powders (e.g., aluminum, stainless steel).
  • suitable additives include fillers such as calcium carbonate, graphite, wollastonite, mica, glass, fiber glass, silica, and tale; inorganic flame retardants such as alumina irihydrate or magnesium hydroxide; organic flame rctardants such as chlorinated or brominat ⁇ d organic compounds; ground construction waste; ground tire rubber; carbon fibers; or metal fibers or powders (e.g., aluminum, stainless steel).
  • These additives can reinforce, extend, or
  • fragrances include fragrances, coupling agents, compalihiiizers, e.g., maleaied polypropylene, processing aids, lubricants, e.g., fluorinated polyethylene, plasticizers, antioxidants, opa ⁇ if ⁇ ers, heat stabilizers, colorants, foaming agents, impact modi tiers, polymers, e.g., degra ⁇ abie polymers, photostabilizers, bi ⁇ ctdes, antistatic agents, e.g., stcarates or ethoxylate ⁇ fatty acid amines.
  • compalihiiizers e.g., maleaied polypropylene
  • processing aids e.g., lubricants, e.g., fluorinated polyethylene, plasticizers, antioxidants, opa ⁇ if ⁇ ers, heat stabilizers, colorants, foaming agents, impact modi tiers, polymers, e.g., degra ⁇ abie polymers, photostabilizers,
  • Suitable antistatic compounds include cond ⁇ etive carbon blacks, carbon fibers, metal fillers, cationie compounds, e.g., quaternary ammonium compounds, e.g., M-(3-di!oro-2-hydroxypropyl)-trirnethyiammonium chloride, alk-inolamJdes, and amines.
  • cationie compounds e.g., quaternary ammonium compounds, e.g., M-(3-di!oro-2-hydroxypropyl)-trirnethyiammonium chloride, alk-inolamJdes, and amines.
  • degradabSe polymers include polyhydroxy acids, e.g., polyiactides, poiyglycolides and copolymers of lactic acid and glycoh ' e acid, polyihydroxybutyric acid), pol y(hydroxyvaicric acid), ⁇ oiy[lactide-co-(e ⁇ capro!aerone ⁇ ], poly[glycolide-co-(e-ca ⁇ r ⁇ lactone ⁇ ], polycarbonates, poly( amino acids), poiylhydroxyalkarsoatejs, po ⁇ yanhydrides, po ⁇ yorthoesters and blends of these polymers.
  • polyhydroxy acids e.g., polyiactides, poiyglycolides and copolymers of lactic acid and glycoh ' e acid, polyihydroxybutyric acid), pol y(hydroxyvaicric acid), ⁇ oiy[lactide-co-(e ⁇ capro!aerone ⁇ ], poly[glycolide-co-(e-ca ⁇ r
  • the fibrous material is sterilized prior to combining with a resin to kill any microorganisms that may be on the fibrous materia!.
  • the fibrous material can be sterilized by exposing the fibrous material to radiation; by heating the fibrous material under conditions and for a sufficient time to kill any microorganisms, e.g., boiling at normal atmospheric pressure; or by employing chemical ster ⁇ anls.
  • Il can h ⁇ advantageous to make the composite smell and/or look like natural wood, e.g., cedarwoo ⁇ .
  • the fragrance e.g., natural wood fragrance
  • the fragrance can be compounded into the resin used to make the composite, in some implementations, the fragrance is compounded directly into the resin as an. oil.
  • the oil can be compounded into the resin using a roll mill, e.g., a Banbury* mixer or an intruder, e.g., _ ⁇ twin-screw extruder with counter-rotating screws.
  • An example of a B anbury" mixer is the F-Seri.es Baabur/' ' mixer, manufactured by Parrel.
  • twin-screw extruder is the WP .ZSK 50 MEGAconipunder iM , manufactured by Kxupp Werner & Pfleiderer.
  • the scented resin can be added to the fibrous materia! and extruded or molded.
  • master batches of fragrance- filled resins are available commercially ⁇ roni international Flavors and Fragrances, under the iradename Poiy!ff i M or ixom the RTP Company, in. some embodiments, the amount of fragrance in the composite is between ab ⁇ us. 0.005 % by weight and about 10 % by weight, e.g., between about 0.1 % and about 5 % or 0.25 % and about 2.5 %.
  • fragrances include evergreen or redwood.
  • Other fragrances include peppermint, cherry, strawberry, peach, lime, spearmint, cinnamon, anise, basil, bergamot, black pepper, camphor, chamomile, citronella, eucalyptus, pine, fir, geranium, ginger, grapefruit, jasmine, juniperberry, lavender, lemon, mandarin, marjoram, musk, myrhb, orange, patchouli, rose, rosemary, sage, sandalwood, tea tree, thyme, vvmtergreen, ykng yiang, vanilla, new car or mixtures of these fragrances.
  • the fibrous material-fragrance combination is between about 0.005 % by weight and about 20 % by weight, e.g., between about 0.1 % and about 5 % or 0.25 % and aboiit 2.5 %, Even other fragrances and methods are described U.S. Provisional
  • any ⁇ f the fibrous material described above, e.g., the first 12 or second fibrous materia! 14, together with a resin can be used to form articles such as pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, hinders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes, crutches, insulation, thread, cloth, novelties, house wares and structures.
  • the fibrous material may be dyed before combining with the resin ami compounding to form the composites described above.
  • this dyeing can be helpful in .masking or biding the fibrous material, especially large agglomerations of the fibrous material, in molded or extruded parts.
  • Such large agglomerations when present in relatively high concentrations, can show up as speckles in the surfaces of the molded or extruded parts.
  • the desired fibrous material can he dyed using an acid dye, direct dye or a reactive dye.
  • dyes are available from Spectra Dyes, Keamy, NJ or Keystone Aniline Corporation, Chicago, IL.
  • Specific examples of dyes include SPECTRATM LIGHT YBLLOW 2G, SPECTRAC1DTM YELLOW 4GL CONC 2C)O 5 SPECTRANYLTM R]-K)DAMIN E S, S PECTRAN YLTM NEUTRAL RED B 5 SPECTRAMINETM BENZOPERPURrNE 5 S PECTRAD IAZ0TM BLACK OB, SPECTRAM ⁇ N£ ⁇ M TURQUOISE G, arid SPECTRAM ⁇ NETM GRBY LVL 200%, each being available from Spectra Dyes,
  • resin color concentrates containing pigments are blended with dyes.
  • the fibrous material may be dyed in-situ during the compounding.
  • Color concentrates are available from €kriant.
  • a 1500 pound skid of virgin, half-gallon juice cartons made of un-pri ⁇ ted polycoaied white Kraft board having a bulk density of 20 Ih /W was obtained from International Paper.
  • the material was cut into pieces 8 i/4 inches by 1 ! inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30, Model SC3G is equipped with four rotary blades, four fixed blades, and a discharge screen having I ⁇ S inch openings.
  • the gap between the rotary and fixed blades was set to approximately 0,020 inch.
  • the rotary knife cutter sheared the confetti -like pieces across the knife-edges, tearing the pieces apart and releasing a fibrous material at a rate of about one pound per hour.
  • the iibrous material had a BET surface area of 0,9748 nr/g +/- 0.0167 rsr/g, a porosity of $9.0437 percent, and a bulk density (@0.53 psia) of 0.1260 g/rnL, An average length of the fibers was 1.141 mm and an average width of the fibers was 0.027 ram, giving an average 1./D of 42; i . Scanning electron micrographs of the fibrous material are shown in Figs, 1 1 and 12 at 25 X magnification and 1000 X magnification, respectively.
  • a 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft' was obtained from International Paper, The materia! was cut into pieces 8 1/4 inches by 1 ! inches using a guillotine cutter and fed to a Munson rotary knife cutler, Model SC30. The discharge screen had 1/8 inch openings. The gap between the rotary and fixed blades was set to approximately 0.020 inch. The rotary knife cutter sheared the confetti -like pieces, releasing a fibrous material at a rate of about one pound per hour.
  • the fibrous material had a BET surface area of i , i 316 trf Vg -*/- 0.0103 m ' V ' g, a porosity of 88.3285 percent and a bulk density (@0.53 psia) of 0.1497 g/mL.
  • Art average length of the fibers was 1 .063 mm and an average width of the fibers was 0,0245 mm. giving an average L/D of 43:1. Scanning electron micrographs of the fibrous material are shown m Figs. 13 and 14 at 25 X inagni fieation and 1000 X magnification, respectively.
  • a 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lbfff was obtained from International Paper, The material was cut into pieces 8 J/4 inches by 11 inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30. The discharge screen had 1/16 inch openings. The gap between the rotary and fixed blades was set to approximately 0,020 inch. The rotary knife cutter the confetti-like pieces, releasing a fibrous material at a rate of about one pound per hour. The material resulting from the first shearing was fed back into the same setup described above aad sheared again. The resulting fibrous materia!
  • a 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 Ib/ft* was obtained from International .Paper.
  • the materia! was cut into pieces B 1 /4 inches by 1 1 inches using a guillotine cutter and fed to a Munso ⁇ rotary knife cutler. Model SC30.
  • the discharge screen had 1/8 inch openings.
  • the gap between the rotary and fixed blades was set io approximately 0.020 inch.
  • the rotary knife cutter sheared the confetti -like pieces across the knife-edges.
  • the material resulting from the first shearing was fed back into the same setup and the screen was replaced with a ⁇ /16 inch screen. This material was sheared.
  • the material resulting from the second shearing was fed back into the same setup and the screen was replaced with a 1/32 inch screen. This material was sheared.
  • the resulting fibrous materia! had a BET surface area of 1.689? nV ⁇ g H-/- 0.0155 ⁇ vVg, a porosity of 87.7163 percent and a balk density (@0.53 psia) of 0.1448 g/mL, An average length of the fibers was 0,824 mm and an average width of the fibers was 0,0262.mm, giving & ⁇ average I../D of 32; 1. Scanning electron micrographs of the fibrous materia! are shown in Figs. 1 ? and 1 8 at 25 X magnification and ICK)O X magnification, respectively,
  • Compositions can be prepared that include any of the fibrous materials described herein, including any of the fibrous materials, resins, additives or oilier components disclosed in U.S. Patent Nos. 6,448,307, 6,258,876, 6.207,729, 5,973,035 ami 5,952,105).
  • any of the fibrous materials described herein can be combined wiih a solid, a liquid or a gas, e.g., a chemical or chemical formulation (m the solid or liquid stale), such as a pharmaceutical (e.g., an antibiotic), an agricultural material (e.g., plant seeds, a fertilizer, herbicide or pesticide), or ars enzyme or a formulation that includes enzymes.
  • a pharmaceutical e.g., an antibiotic
  • an agricultural material e.g., plant seeds, a fertilizer, herbicide or pesticide
  • ars enzyme or a formulation that includes enzymes e.g., ars enzyme or a formulation that includes enzymes.
  • Compositions that include one or more type of bacteria or bacteria m combination with one or more enzymes can also be prepared.
  • any of the fibrous materials can be used to absorb chemicals, potentially absorbing many times their own weight.
  • the fibrous materials can be used to absorb spilled oil, or other chemicals.
  • Combining these fibrous materials with a microorganism, such as a bacterium, that can metabolize the oil or chemical can aid in cleanup.
  • the fibrous materials can be combined with solutions of enzymes, dried, and then used in pet bedding, or combined with a pharmaceutical and used for delivering a therapeutic agent, such as a drug.
  • the fibrous materials can be combined with a degradabie polymer, e.g., polyglyeolic acid, polylactic acid ami copolymers of glyeoiic and lactic acid.
  • a degradabie polymer e.g., polyglyeolic acid, polylactic acid ami copolymers of glyeoiic and lactic acid.
  • Other degradabie materials that can be used have been discussed above,
  • compositions that include fibrous materials, e.g., celluiosie or Ugnoeeilulosie materials and, e.g., chemicals or chemical formulations in the solid, liquid or gaseous slate, can be prepared, e.g., in various immersion, spraying, or blending apparatuses.
  • the compositions can be prepared using ribbon blenders, cone blenders, double cone blenders, and Patterson-Kelly "V" blenders.
  • ⁇ gnin can be removed from any of the fibrous materials feat include lignin, such as Hgnocellalosic materials.
  • the fibrous materia! can. be sterilized to kill any microorganisms that may be on the fibrous material.
  • the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation.
  • radiation such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation.
  • the fibrous materials can also be sterilized by healing the fibrous material under conditions and for a sufficient time to kill any microorganisms, or by employing a chemical sterila ⁇ t, such as bleach (e.g., sodium hypochlorite), chlorhexidine, or ethylene oxide.
  • bleach e.g., sodium hypochlorite
  • chlorhexidine e.g., chlorhexidine
  • ethylene oxide ethylene oxide
  • the fibrous materials cat) be used as a feedstock for various microorganisms, such as yeast and bacteria, that can ferment or otherwise work on the fibrous mate ⁇ ais to produce a useful materia!, such as a fuel, e,g,, an alcohol, an organic acid, a hydrocarbon or hydrogen, or a protein.
  • a fuel e,g,, an alcohol, an organic acid, a hydrocarbon or hydrogen, or a protein.
  • the alcohol produced can be a monohydroxy alcohol e.g., ethanol. or a polyhydroxy alcohol, e.g., ethylene glycol or glycerin.
  • examples of alcohols that can be produced include methanol, ethanol ,. propanoi, isopropanol, butatioK ethylene glycol,
  • the organic aci ⁇ produced can a monocarboxylic acid or a polycarboxylie acid.
  • organic acids include formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproie, palmitic acid, stearic acid, oxalic acid, rnakmic acid, succinic acid, giutaric acid, oleic acid, ii ⁇ oleie acid, glycolic acid, lactic acid, ⁇ hydroxybutyric acid or mixtures of these acids.
  • the hydrocarbon produced can be, e,g., an alkane or an. aikene. Examples of hydrocarbons thai can be produced include methane, ethane, propane, isobntene, pentane, n-hexane or mixtures of these hydrocarbons.
  • a fiber source that includes a eellulosie and/or iignoceliul ⁇ sic iiber source is sheared to provide a first fibrous material.
  • the first fibrous material is then passed through a first screen having an average opening size of about 1.59 mm or less (1/16 inch, 0.0625 inch) to provide a second fibrous material.
  • the second fibrous material is combined with a bacterium and/or enzyme, in this particular embodiment, the bacterium and/or enzyme is capable of utilizing ⁇ he second librous materia! directly without pre-treatraent to produce a fuel that includes hydrogen, an. alcohol, an organic acid and/or a hydrocarbon.
  • the fibrous material prior to combining the bacteria and/or enzyme, is sterilized to kill any microorganisms that may be on the fibrous material.
  • the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation.
  • radiation such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation.
  • the microorganisms can also be killed using chemical steriianls, such as bleach (e.g., sodium hypochlorite), ehlorhexidine, or ethylene oxide.
  • the cellulosic and/or KgnoceHu ⁇ osic material ofthe fibrous material is Container broken, down into lower molecular weight sugars, which are then added to a solution of yeast and/or bacteria that ferment the lower molecular weight sugars to produce ethatio!.
  • the cellulosic and/or lignocell ⁇ losic material can be broken down using chemicals, such as acids or bases, by enzymes, or by a combination of the two. Chemical hydrolysis of cellulosic materials is described by Bjerre, in BiotechnoL Bioeng,, 49:568 (1996) and Kim in Biotechnal. Prog,, 18:489 (2002), which are each hereby incorporated by reference herein in their entirety,
  • a fibrous material having a low hulk density can be combined with a microorganism, e.g., freeze-dried yeast or bacteria, and/or a enzyme, and then revertibly densif ⁇ ed to a fibrous material composition having a higher bulk density.
  • a fibrous material composition having a bulk density of 0.05 g/ cm* can be dc ⁇ sified by sealing the fibrous material in a relatively gas impermeable structure, e.g., a bag made of polyethylene or a bag made of alternating layers of polyethylene and a nylon, and then evacuating the entrapped gas, e.g., air, from the structure.
  • the fibrous material can have, e.g., a bulk density of greater than 0.3 g/c ⁇ v ⁇ e.g., 0.5 g/cnV, 0.6 g/enr ⁇ 0.7 g/cm J or more, e.g., 0.85 g/ crsr'.
  • a bulk density of greater than 0.3 g/c ⁇ v ⁇ e.g., 0.5 g/cnV, 0.6 g/enr ⁇ 0.7 g/cm J or more, e.g., 0.85 g/ crsr'.
  • This can be advantageous when it is desirable to transport the fibrous material Io another location, e.g., a remote manufacturing plant, where the fibrous material composition can be added to a solution, eg,, to produce ethanol.
  • the dens ⁇ ied fibrous material After piercing the substantially gas impermeable structure, the dens ⁇ ied fibrous material reverts to nearly its initial bulk density, e.g., greater than 60 percent of its initial bulk density, e.g., 70 percent, 80 percent. 85 percent or more, e.g., 95 percent of its initial bulk density.
  • an anti-static agent can be added to the fibrous material.
  • a chemical anti-static compound e.g., a canonic compound, e.g., quaternary ammonium compound, can be added to the fibrous material
  • the structure e.g., bag
  • the structure is formed of a material, that dissolves in a liquid, such as water.
  • the structure can be formed from a polyvinyl alcohol so that it dissolves when in contact with a wafer-based system.
  • densif ⁇ ed structures to be added directly to solutions, e.g., that include a microorganism, without first releasing the contents of the structure, e.g.. by cutting.
  • a fiber source is sheared between a first pair of blades that defines a first gap, resulting in a first fibrous material.
  • the first fibrous material is then sheared between a second pair of blades: that define a second gap that is smaller than the first gap, resulting in a second fibrous material.
  • Similar screening processes can be repeated as many rimes as desired to produce the desired fibrous material having the desired properties.
  • a ratio of an average length-to-diameter ratio of the first fibrous material to an average length-to-diameter of the second fibrous material is less than 1.5

Abstract

This invention relates to the fibrous mateπals, methods of making fibrous materials, compositions that include fibrous materials and a resin, or compositions that included the fibrous materials and bacteria and/or enzymes In addition, the use of the fibrous materials compositions are disclosed. For example, the fibrous materials can be operated on by a microorganism to produce a fuel compnsing hydrogen, an alcohol such as ethanol, an organic acid and/or hydrocarbon

Description

FIBROUS MATERIALS AND COMPOSITIONS
CROSS REFERENCE TO RELATED APPLICATIONS 'This application claims the benefit of priority from U.S. Patent Application Serial No. i 1/453,951 , like! June 15, 2006, the entire contents of which is hereby incorporated by reference herein in its entirety.
TECHNICAL FIELD
This invention relates to fibrous materials and to compositions.
BACKGROUND
Fibrous materials, e.g., ceHuIosic arid IignoccHuiosic materials, are produced, processed, and used in large quantities in a number of applications. Often such fibrous materials are ust-ά once, and then discarded as waste.
Various fibrous materials, their uses and applications have been described in U.S. Patent Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105. The entire disclosure of each of the patents of this paragraph is incorporated by reference herein.
SUMMARY
Generally, this invention relates to fibrous materials, methods of making fibrous materials, compositions that include fibrous materials (e.g.. composites that include the fibrous materials and a resin, or compositions that include the fibrous materials and bacteria and/or an enzyme), and to uses of the same. For example, the compositions car: be used to make ethauoi, or a by-product, such as a protein or ligrmi, or applied to a structure as insulation.
Any of the fibrous materials disclosed herein can be used in combination with, any of the fibrous materials, resins, additives, or other components disclosed in U.S. Patent Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105. Tn turn, these fibrous materials and/or components can be used in any of the applications, products, procedures, et cetera disclosed in any of these patents or in this application.
The fibrous materials or compositions thai include the fibrous materials can be, e.g., associated with, blended with, adjacent to, surrounded by, or within a structure or carrier (eg., a netting, a membrane, a flotation device, a bag, a shell, or a biodegradable substance). Optionally, the structure or carrier may itself be made from a fibrous materia!, or of a composition that includes a fibrous material, In some embodiments, the fibrous material is combined wiύi a material, such as a protic acid, that enhances the rate of biodegradatioπ of the fibrous material In some embodiments, the fibrous materia! is combined with a material that retards degradation of the fibrous material, such as a buffer.
The ratio of fibrous materials to the other components of the compositions will depend upon the nature of the components, and can be readily adjusted for a specific product application.
Any of the fibrous materials described herein, including any of the fibrous materials made by asiy of the methods described herein, can be used, e.g., to form composites with resin, or can be combined with bacteria and/or one or more enzymes to produce a valuable product, such as a fuel (e.g., ethaπoL a hydrocarbon, or hydrogen).
In one aspect, the invention features methods of making fibrous materials. The methods include shearing & fiber source to provide a first fibrous material, and passing the first fibrous material through a Erst screen having an average opening size of 1.59 mm or less ( L' 16 inch. 0.0625 inch) to provide a second fibrous material. The fiber .source can, e.g., be cut into pieces or strips of confetti-like material prior to the shearing. hi some embodiments, the average opening size of the first screen is less than 0.79 mm (1/32 inch, 0.03125 inch), e.g., less than 0.40 mm ( 1/64 inch, 0.015625 inch), less fa 0.20 ram (1/128 inch, 0.007S 125 inch), or even less than 0.10 mm (1/256 inch, 0.00390625 inch}, hi specific implementations, the shearing is performed with a rotary knife cutter. If desired, the shearing can be performed while the fiber source is dry (e.g., having leas than 0.25 percent by weight absorbed water), hydrated, or even while the fiber source is partially or fully submerged in a liquid, such as water or isopropariol.
The second fibrous material can, e.g., be collected in a bin having a pressure below nominal atmospheric pressure, e.g., at least H) percent below nominal atmospheric pressure, at least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure. The second fibrous material can, e.g., be sheared once or numerous times, e.g., twice, thrice, or even more, e.g., ten times. Shearing can "open up" and/or "stress" the fibrous materials, making the materials more disperssbie, e.g., in a solution or in a resin. The second fibrous material can be, e.g., sheared and the resulting fibrous material passed through the iirsi screen.
The second fibrous material can be sheared, and the resulting fibrous material passed through a second screen having an average opening size less than the first screen, providing a third fibrous material
A ratio of an average length-to-diameter ratio of the second fibrous material to an average fength-io-diameter ratio of the third fibrous materia! ears, be, e.g., less than 1.5, less than i .4, less than 1.25, or even less thai 1.1.
The second fibrous can be, e.g., passed through a second screen having an average opening size less than the first screen.
The shearing and passing can be, e.g., performed concurrently.
The second fibrous material can have an average Jengih-to-diameter ratio of, e.g.. greater than H)Zi , greater than 25/ i , or even greater than 50/1.
For example, an average length of the second fibrous material can be between 0,5 mm and 2.5 ram, e.g., between 0.75 mm and LO mm. For example, an average width of the second fibrous material can be between 5 μm and 50 μrrs, e.g., between 10 μm and 30 μm,
A Standard deviation of a length of the second fibrous material can be less than 60 percent of an average length of the second fibrous material, e.g., less than. 50 percent of an average length of the second fibrous materia!. in some embodiments, a BBT surface area of the second fibrous material is greater t'hart 0.5 nr/g, e.g., greater than l .ϋ πr/g, greater than 1.5 m'7g, greater than 1,75 πϊ; /g, greater than 2,5 rrr/g, greater than 10.0 mVg, greater than 25.0 Tn-Vg, greater than 50.0 nr/g, or even greater than 100.0 m7g.
In some embodiments, a porosity of the second fibrous material is greater than 25 percent, e.g., greater than 50 percent, greater than 75 percent, greater than SS percent, greater than 90 percent, greater than 92 percent, greater than 95 percent, or even greater than 99 percent.
In specific embodiments, the screen is formed by interweaving monofilaments.
The fiber source cars, include, e.g., a ecHulosie material a lignoeeϋulosk material. in some embodiments, the liber source includes a blend of fibers, e.g., fibers derived from a paper source and fibers derived from a textile source, e.g., cotton. m another aspect, the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; and passing the fibrous materia! through a first screen to provide a second fibrous materia!. A ratio of an average lengϋi-to-diametcr ratio of the first fibrous material to an average length-to-diamcter of the second fibrous material is less than 1.5.
In another aspect, the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; passing the fibrous material through a first screen to provide a second fibrous material; and then shearing the second fibrous material again to provide a third fibrous materia], hi another aspect, the invention features composites or compositions made from any of the fibrous materials described herein. For example, compositions can include any of the fibrous materials described herein and a bacterium and/or an enzyme. The compositions thai include any of the fibrous materials described herein and die bacterium and/or enzyme can be in. a dry state, or they can include a liquid, such as water.
For example, the composite can be in the form of a stepping stool, pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, iool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings., above- axsd below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, bangers, servers, caskets, book covers, canes and cratches.
IB another aspect, the invention features fibrous materials having an average length- to-diametεr ratio of greater than 5, and having a standard deviation of a fiber length of less than sixty percent of an average fiber length.
For example, the average leπgth-to~diameter ratio can be greater than 10/1 , e.g., greater than 15/1 , greater than 25/1 , greater than 35/1 , greater than 45/1 , or even greater than 50/1.
For example, she average length can be between 0.5 mm and 2,5 mm. In another aspect, the invention features methods of making fibrous materials that include shearing a liber source to provide a first fibrous material; collecting the first fibrous material; and then shearing the first fibrous to provide a second fibrous material
In another aspect, the invention features methods of making a useful material, such as a fuel. The methods include shearing a fiber source to provide a First fibrous material; passing the first fibrous materia! through a first screen having an average opening size of about 1.59 mm or less (1/16 inch, 0,0625 inch) to provide a second fibrous materia!; and combining the second fibrous material with a bacterium and/or enzyme> the bacterium and/or enzyme utilizing the second fibrous material to produce a fuel that includes hydrogen, an alcohol, an organic acid and/or a hydrocarbon, The alcohol can be, e.g., methanol, ethanoL propanoic isopropaπoL butanol, ethylene glycol, propylene glycol, 1, 4-hutane dial, glycerin, or mixtures of these alcohols; the organic acid can be, e.g., malomc acid, succinic acid, glutaric acid, oleic acid, liriolek acid, glycolic add, lactic acid, γ-hydroxybutyric acid, or mixtures of these acids; and the hydrocarbon can be, e.g., methane, ethane, propane, isohutεne, pentaπe. π~hcxane, or mixtures of these hydrocarbons.
Prior to combining with the bacterium and/or enzyme, any of the fibrous materials described herein can be hydrolyzed to break down higher molecular weight carbohydrates ink) lower molecular weight carbohydrates. in another aspect, the invention features methods of making a useful material, such as a fuel, by shearing a, liber source or a fibrous material, and then combining if with a bacterium and/or an enzyme. For example, the fiber source can be sheared once to provide a fibrous material, arid then the fibrous material can be combined with a bacterium and/or an eiixyrne to make the useful material.
In another aspect, the invention features methods of deπsϊfying fibrous compositions. The methods include shearing a fiber source to provide a fibrous material; combining the fibrous material with a bacterium and/or enzyme to provide a fibrous material composition: encapsulating the composition in a substantially gas impermeable materia!; find removing entrapped gas from the encapsulated composition to densify the composition. For example, the gas impermeable material can be in the form of a bag, and. the composition can be deasified by evacuating air from the bag, and then sealing the bag. hi another aspect, the invention features composites that include s fibrous material, a resin and a dye.
For example, the fibrous material can have an average lengih-to-diaincter ratio of greater than 5, and a standard deviation of a liber length of less than sixty percent of an average fiber length,
In some embodiments, the composite additionally includes a pigment, ϊn some implementations, the dye soaked into or surfaced on the fibers. In another aspect, the invention, features methods of making composites that include dyeing a fibrous material; combining the fibrous material with a resin; and forming a composite from the combination,
Irs another aspect, the invention features methods of making composite ihat include adding a dye to a resin to provide a dye/resin combination; combining the dye/resin combination with a fibrous material; and forming a composite from the dye/resin combination and fibrous material
The term "Ebrous material", as used herein, is a material thai includes numerous loose, discrete and separable fibers. For example, a fibrous material can be prepared from a polycoated paper or a bleached Kraft paper fiber source by shearing, e.g., with a rotary knife cutter.
The term "screen", as used herein, means a member capable of sieving material according to size, e.g., a perforated plate, cylinder or the like, or a wire mesh or cloth fabric. Embodiments and/or aspects can have any one of, or combinations of, the following advantages. The fibrous materials axe opened up and/or stressed, making the materials more dispcrsible, e.g., in a solution or in a resin, and making them more susceptible to chemical, enzymatic or biological attack. The fibrous materials can have, e.g., a relatively narrow length and/or iength-to-diameter ratio distribution, such that their properties are consistently defined. For example, when blended with a molten resin or a solution, the fibers of the fibrous materials can modify the rheology of the molten resin, or solution in a consistent and predieable manner, e.g., resulting in resin/fibrous material combinations that are, e.g., easier to mold and extrude. For example, the fibrous materials can easily pass through small openings or channels, such as those found in or associated with injection molds, e.g., gates or hot runners. Paris molded from such fibrous materials can exhibit a good surface finish, e.g., with few visible speckles of large particles and/or agglomerated particles,
All publications, patent applications, patents, and other references mentioned herein are incorporated by reference in their entirety for all that they contain.
Other features and advantages of the invention will be apparent from the following detailed description, and from the claims.
DESCRIPTION OF DRAWINGS
Fig. 1 is block diagram illustrating conversion of a fiber source into a first and second fibrous material. Fig, 2 is a cross-sectional view of a rotary knife cutter, figs. 3-8 are top views of a variety of screens made from monofilaments.
Fig. 9 is block diagram illustrating conversion of a fiber source into a first, second and third fibrous material.
Figs. 1OA arid 1OB are photographs of fiber sources; Fig, iOA being a photograph of a polyeoated paper container, and Fig, 1 OB being a photograph of unbleached Kraft paper rolls.
-1 as. ! and 12 are scanning electron micrographs of a fibrous materia! produced from polycoa .ed paper at 25 X magnification and 1000 X magnification, respectively. The fibrous mater! al was produced on a rotary knife cutter utilizing a screen with i /S inch openings.
Figs. 13 arκl 14 are scanning electron micrographs of a fibrous material produced from bleached Kraft, board paper at 25 X magnification and IC1OO X magnification, respectively. The iibrøi-s material was produced on a rotary knife cutter utilizing a screen with 1/8 inch openings.
Figs. 15 and 16 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 X magnification and ! 0OO X magnification, respectively. The fibrous material was twice sheared on a rotary knife cutter utilizing a screen with l/' i δ inch openings during each shearing. Figs, 17 and 18 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 X magnification and 1 OCl(J X magnification, respectively. The fibrous material was thrice sheared on a rotary knife c utter. During the first shearing, a 1/8 inch screen was used; during the second shearing, a 1/16 inch screen was used, and during the third shearing a 1 /32 inch screen was used. fig. 19 is a block diagram illustrating revertible bulk densifieaiion of a fibrous materia! composition.
DETAILED DESCRIPTION
Referring to Fig, i , a fiber source 10 is sheared, e.g., in a rotary knife cutter, to provide a iirsi fibrous materia] 12. The first fibrous material 12 is passed through a first screen 16 having an average opening size of 1 ,59 mm or less (1 /16 inch, 0.0625 inch) to provide a second fibrous material .14, if desired, fiber source 10 can be cut prior to the shearing, e.g , with a shredder. Pot example, when a paper is used as the fiber source the paper can be first cut into strips that are, e.g., 1/4- to 1/2-inch wide, using a shredder, e.g., a counter-rotating screw shredder, such as those manufactured by Munson (Utica, N. Y.). As an alternative to shredding, the paper can be reduced in size by catting to a desired size using a guillotine cutter. For example, the guillotine cotter cars be used to cut the paper irsio sheets that are, e.g., 10 inches wide by 12 inches long.
In some embodiments, the shearing of fiber source 10 and the passing of the resulting first tibrous material 12 through first screen 16 are performed concurrently. The shearing and the passing can also be performed in a batch-type process.
For example, a rotary knife carter can he used to concurrently shear the fiber source 1 (I and screen the first fibrous materia! 12, Referring to Fig. 2, a rotary knife cutter 20 includes a hopper 22 that can be loaded with a shredded fiber source H)" prepared by shredding iϊbcr source 10. Shredded fiber source i 0' is sheared between stationary blades 24 and rotating blades 26 to provide a first fibrous material 12, First fibrous material 12 passes through screen 16 having the dimensions described above, and the resulting second fibrous material 14 is captured in bin 30. To aid in the collection of the second fibrous material 14, bin 30 can have a pressure below nominal atmospheric pressure, e.g., at least 10 percent below nominal atmospheric pressure, e.g., at least 25 percent below nominal atmospheric pressure, ni least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure, In some embodiments, a vacuum source 50 (Fig, 2) is utilized to maintain the bin below nominal atmospheric pressure.
Shearing can be advantageous for "opening up" and "stressing" the fibrous materials, making the materials more dispersible, e.g., in a solution or in a resin, and making them more susceptible to chemical, enzymatic or biologies! attack. Without wishing to be bound by any particular theory, it is believed, at least in some embodiments, that shearing can iiinciionalize fiber surfaces with functional groups, such as hydroxy! or carboxylic acid groups, which can, e.g., help disperse the fibers in a molten resin or enhance chemical or biological attack.
"The fiber source can be sheared in a dry state, a liydrated state (e.g., having up to ten percent by weight absorbed water), or in a wet state, e.g., having between about i 0 percent and about 75 percent by weight, water. The fiber source can even be sheared while partial iy or fully submerged under a iiqnid, such as water, efhanoL isopropanol.
The fiber source can also be sheared in under a gas (such as a stream or atmosphere of gas other than air), e.g., oxygen or nitrogen, or steam. Other methods of making the fibrous materials include stone grinding, mechanical ripping or tearing, pin grinding or air attrition nulling.
If desired, the fibrous materials can be separated, e.g., continuously or in batches, into fractions according to their length, width, density, material type, or some combination of these attributes. For example, for forming composites, it is often desirable to have a relatively narrow distribution of fiber lengths. In addition, e.g., when making compositions that include bacteria and/or an enzyme, it is often desirable to use a substantially single material as a feedstock.
For example, ferrous materials can be separated from any of the fibrous materials by passing a fibrous material that includes a ferrous materia] past a magnet, e.g., an electromagnet, and then passing the resulting fibrous material through a series of screens, each screen having different sized apertures.
The fibrous materials can also be separated, e.g., by using a high velocity gas, e.g., air. in such an approach, the fibrous materials are separated by drawing off different fractions, which can be characterized photonic-ally, if desired. Such a separation apparatus is discussed in Lindsey et a!, U.S. Patent No. 6,883,667, the entire disclosure of which is hereby incorporated by reference herein in its entirety.
'The fibrous materials can be used immediately following their preparation, or they can may be dried, e.g.. at approximately 105 °C for 4-18 hours, so that the moisture content is, e.g., less than about 0.5% before use.
If desired, lignin can be removed from any of the fibrous materials that include H gain, such as Hgnoedlulosie materials. Also, if desired, the fibrous material can be sterilized Io kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilised by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation. The 'fibrous materials can also be sterilized by temperature adjustment, e.g., heating or cooling fee fibrous material under conditions and for a sufficient time to kill any microorganisms, or by employing a chemical sterilant, such as bleach (e.g., sodium hypochlorite), ehlorhexidine, or ethylene oxide. The fibrous materials can also be sterilized by using a competitive organism, such as yeast against bacteria.
Referring to Figs. 3-S, in some embodiments, the average opening SΪKC of the first screen 16 is less than 0.79 mm (1/32 inch, 0.03125 inch), e.g., less than (3.51 mm (1/50 inch, 0,02000 inch), less than 0.40 rπm (1/64 inch, 0,01 S625 inch), less than 0.23 mm (0.009 inch), less than 0.20 ram (1/128 inch, 0,0078125 inch). less than O.I S mm (0.007 inch), less than 0.13 mm (0,005 inch), or even less than less than 0.10 mm (1/256 inch, 0.00390625 inch). Screen 16 is prepared by interweaving monofilaments 52 having an appropriate diameter to give the desired opening size. For example, the monofilaments can he made of a metal, e.g., .stainless steel. As the opening sizes get smaller, structural demands o.n the monofilaments may become greater. For example, for opening sizes less than 0.40 mm, it can !>ε advantageous to make the screens from .monofilaments made from a material other than stainless steel, e.g.. titanium, titanium alloys, amorphous metals, nickel tungsten, rhodium, rhenium, ceramics, or glass. In some embodiments, the screen is made {mm a plate, e.g. a metal plats, having apertures, e.g., cut into the plate using a laser.
In some embodiments, the second fibrous 14 is sheared and passed through the first screen 16, or a different sized screen, In some embodiments, the second fibrous material 14 is passed through a second screen having an average opening size equal to or less than that of first screen HS. Referring to Fig. 9, a third fibrous material 62 can be prepared from the second fibrous materia] 14 by shearing the second fibrous material 14 and passing the resulting materia! through a second screen 60 having an average opening sixe !©ss than the first screen 16.
Fiber sources include eelkdosie liber sources, incmding paper and paper products like those shown in Figs. ISA (polyeoaied paper) and 1OB (Kraft paper), and iigπocellulosic liber sources, including wood, and wood-related materials, e.g., particle board. Other suitable fiber sources include natural fiber sources, e.g., grasses, rice hulls, bagasse, co.toπ, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, rice bulls, coconut hair; fiber sources high in α-ceJluiose content, e.g., cotton; synthetic fiber sources, e.g., extruded yam (oriented yam or usi-oriented yam) or carbon fiber sources; inorganic fiber sources; and metal fiber sources. Natural or synthetic fiber sources can be obtained from virgin scrap textile materials, e.g., remnants or they can be post consumer waste, e.g., rags. When paper products are used as fiber sources, they can be virgin materials, e.g., scrap virgin materials, or they can be past-consumer waste. Aside from virgin raw materials, post-consumer, industrial (e.g., offal), and processing waste (e.g., effluent from paper processing) can also be used as fiber sources. Also, the fiber source can be obtained or derived from human (e.g., sewage), animal or plant wastes. Additional fiber sources have been described in U.S. Patent Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 aid 5,952,105, each of which is incorporated by reference herein in its entirety.
Blends of any of the above fibrous sources may be used. Generally, the fibers of the fibrous materials can have a relatively large average length-to-diameier ratio (e.g., greater than 2(Ro-I), even if they liavt- been sheared more lhayj once. Fn addition, the fibers of the fibrous materials described herein may have a relatively narrow length and/or length-to-diameter ratio distribution. Without wishing to be bound by any particular theory, it is currently believed that the relatively large average fength-to-diameter ratio and the relatively narrow length and/or length -to-diameter ratio distribution are, at least in part, responsible for the ease at which the fibrous materials are dispersed in a resin, e.g., a molten thermoplastic resin. It is also believed that the relatively large average length-to-diameter ratio and the relatively narrow length and/or ieπglh-to- dia÷meiεr ratio distribution are, at least in part, responsible for the consistent properties of the fibrous materials, the predictable rheoiogy modification the fibrous materials impart on a resin, the ease at which the combinations of the fibrous materials and resins are east, extruded and injection molded, the ease in which the fibrous materials pass through small, often torturous channels and openings, and the excellent surface finishes possible with molded parts, e.g., glossy finishes and/or finishes substantially devoid of visible speckles. As used herein, average fiber widths (i.e., diameters) are those determined optically by randomly selecting approximately 5,000 fibers. Average liber lengths are corrected length-weighted lengths, BET (Bmnauer, Emmet and Teller) surface areas are multi-point surface areas, arid porosities are those determined by mercury porosπnetry.
The average length-to-diameler ratio of the second fibrous material 14 can be, e.g. greater than 8/1, e.g,, greater than 10/1, greater than 15/1, greater than 20/1, greater than 25/1, or greater than 50/ J . An average length of the second fibrous material 14 can be, e.g., between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 mm, and an average width (i.e., diameter) of the second fibrous material 14 can be, e.g.. between about 5 μm and 50 μmf e.g., between about K) μm and 30 μm.
In some embodiments, a standard deviation of the length of the second fibrous material 14 is less than 60 percent of an average length of the second fibrous material 14, e.g., less than 50 percent of the average length, less than 40 percent of the average length, less than 25 percent of the average length, less than 10 percent of the average length, less th&n 5 percent of the average length, or even less than 1 percent of the average length. π In some embodiments, a BET surface area of the second fibrous materia! 14 is greater than. O.I m7g, e.g., greater than 0.25 rrΛ'g, greater than 0.5 m2/g, greater than 1.0 nr/g, greater than 1.5 m'/g, greater than 1.75 rrπ'g, greater than 5.0 πr/g, greater than 10 mv'g, greater than 25 m"/g, greater than 35 nr/g, greater than 50.rrf /g, greater than 60 rrr/g, greater than 75 πr/g, greater than 100 m'Vg, greater than 150 πr/g, greater than 200 nr/g, or even greater than 250 nr/g. A porosity of the second fibrous material 14 can be, e.g., greater than 20 percent, greater than.25 percent, greater than 35 percent, greater than 50 percent, greater than 60 percent, greater than 70 percent, e.g., greater than 80 percent, greater than. 85 percent, greater than 90 percent, greater than 92 percent, greater than 94 percent, greater than SKS percent, greater than 97,5 percent, greater than 99 percent; or even greater than 99.5 percent. in some embodiments, a ratio of the average leπgth-to- diameter ratio of the first fibrous material 12 to the average lengtb-to-diaraeter ratio of the second ribrous material 14 is, e.g., less than ! .S, e.g., less than 1.4, less than 1.25, less than U, less than ! .075, less than 1.05, less than 1.025, or even substantially equal to L
In particular embodiments, the second fibrous material 14 is sheared again and the resulting fibrous materia! passed through a second screen having an average opening size less than the first screen to provide a third fibrous material 62. In such instances, a ratio of the average length-to-diameter ratio of the second fibrous material 14 to the average length- to-diameier ratio of the third fibrous material 62 can be, e.g., less than 1.5, e.g., less than 1 ,4, less than 1.25, or even less than 1.1.
In some embodiments, the- third fibrous material 62 is passed through a ihirtl screen to produce a fourth fibrous material. 'Hie fourth fibrous material can be, e.g., passed through a fourth screen to produce a fifth material Similar screening processes can be repeated as many times as desired to produce the desired fibrous material having the desired properties.
Is some embodiments, the desired fibrous material includes fibers having art average lersgth-to-di&meter ratio of greater than 5 and having a standard deviation of the fiber length that is less than sixty percent of the average length. For example, the average length-to- diameter ratio can be greater than 10/ 1 , e.g., greater than 25/1 , or greater than 50/ 1 , and the average length can be between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 roxn. An average width of the fibrous material can be between about 5 μro and 50 μre, e.g.. between about 10 μm and 30 μm. For example, the standard deviation can be less than 50 percent of the average length, e.g., less than 40 percent, less than 30 percent, less than 25 percent, less than 20 percent, less than 10 percent, less than 5 percent, or even less than 1 percent of the average length. A desirable fibrous material can have, e.g., a BET surface area of greater than 0.5 rrf/g, e.g., greater than 1.O nYVg, greater than 1.5 πϊ7g, greater th&n 1.75 rn/Vg., greater than 5 m2/g, greater than 10 m"7g, greater than 25.0 rrr/g, greater than 50,0 rrr/g, greater than 75.0 nr/g, or even greater than 100.0 m"/g. A desired material can have, e.g., a porosity of greater than 70 percent, e.g., greater than 80 percent, greater than 87.5 percent, greater than 90 percent, greater than 92.5, greater than 95, greater than 97.5, or even greater than 99 percent. A particularly preferred embodiment has a BET surface area of greater than 1.25 rrf/g and a porosity of greater than 85 percent.
Composites including any of the fibrous materials or blends of any of the fibrous materials described herein (including any of the fibrous materials disclosed in Ii, S. Patent Nos, 6,448,307, 6,258.876, 6,207,729, 5,973,035 and 5,952,105), e.g., the first 12 or second fibrous materia! 14, and a resin, e.g., a thermoplastic resin or a thermosetting resin, ears be prepared by combining the desired fibrous materia! and the desired resin. The desired fibrous material can he combined with the desired resin, e.g., by mixing the fibrous material and the resin in an. extruder or other mixer, Ib form the composite, the fibrous material can be combined with the resin as the "fibrous materia! itself or as a deπsifieά fibrous material that can be re-opened during the combining. Such a densilied material is discussed in international Application No. PCT/US2006/010648, filed on March 23, 2006, the disclosure of which is incorporated herein by reference in its entirety.
Examples of thermoplastic resins inciude rigid and elasSomeric thermoplastics. Rigid thermoplastics include polyolefins (e.g., polyethylene, polypropylene, or polyolefni copolymers), polyesters (e.g., polyethylene terephthakte), poiyamidcs (e.g., nylon 6, 6/12 or 6/10), and polyethyieneirnines. Examples of ekstomerie thermoplastic resins include elastorøeric siyreme copolymers (e.g.. styrene-ethyiene-butyleαe-styrene copolymers), pαlyaπride elastomers (e.g., poiyether-polyamide copolymers) and ethyl εne-vinyl acetaie copolymer.
In some embodiments, the thermoplastic resin has a melt Sow rate of between IO g/10 minutes to ό'O g/10 minutes, e.g., between 20 g/10 minutes to 50 g/10 minutes, or between 30 g/30 minυtes to 45 g/10 minutes, as measured αsiπg ASTM 123 S. In some embodiments, compatible blends of any of the above thermoplastic resins cars be used,
In some embodiments, the thermoplastic resin has a polydispersiiy index (PDf), i.e., a ratio of the weight average molecular weight to the number average molecular weight, of greater thim 1.5, e.g., greater than 2.0, greater than 2.5, greater than 5,0. greater than 7.5, or even greater than .10.0. in specific embodiments, polyoiefiαs or blends of pol yolefms are utilized as the thermoplastic resin.
Examples of thermosetting resins include natural rubber, butadiene-rubber and polyurethanes.
In addkioα Io the desired fibrous material and resin, additives, e.g., in the form of a solid or a liquid, can be added to the combination of the fibrous material and resin. For example, suitable additives include fillers such as calcium carbonate, graphite, wollastonite, mica, glass, fiber glass, silica, and tale; inorganic flame retardants such as alumina irihydrate or magnesium hydroxide; organic flame rctardants such as chlorinated or brominatεd organic compounds; ground construction waste; ground tire rubber; carbon fibers; or metal fibers or powders (e.g., aluminum, stainless steel). These additives can reinforce, extend, or change electrical, mechanical or compatibility properties. Other additives include fragrances, coupling agents, compalihiiizers, e.g., maleaied polypropylene, processing aids, lubricants, e.g., fluorinated polyethylene, plasticizers, antioxidants, opaεifϊers, heat stabilizers, colorants, foaming agents, impact modi tiers, polymers, e.g., degraάabie polymers, photostabilizers, biαctdes, antistatic agents, e.g., stcarates or ethoxylateά fatty acid amines. Suitable antistatic compounds include condυetive carbon blacks, carbon fibers, metal fillers, cationie compounds, e.g., quaternary ammonium compounds, e.g., M-(3-di!oro-2-hydroxypropyl)-trirnethyiammonium chloride, alk-inolamJdes, and amines. Representative degradabSe polymers include polyhydroxy acids, e.g., polyiactides, poiyglycolides and copolymers of lactic acid and glycoh'e acid, polyihydroxybutyric acid), pol y(hydroxyvaicric acid), ρoiy[lactide-co-(e~capro!aerone}], poly[glycolide-co-(e-caρrø lactone}], polycarbonates, poly( amino acids), poiylhydroxyalkarsoatejs, poϊyanhydrides, poϊyorthoesters and blends of these polymers.
In some embodiments, the fibrous material is sterilized prior to combining with a resin to kill any microorganisms that may be on the fibrous materia!. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation; by heating the fibrous material under conditions and for a sufficient time to kill any microorganisms, e.g., boiling at normal atmospheric pressure; or by employing chemical sterϋanls.
Il can hε advantageous to make the composite smell and/or look like natural wood, e.g., cedarwooά. For example, the fragrance, e.g., natural wood fragrance, can be compounded into the resin used to make the composite, in some implementations, the fragrance is compounded directly into the resin as an. oil. For example, the oil can be compounded into the resin using a roll mill, e.g., a Banbury* mixer or an intruder, e.g., _ι twin-screw extruder with counter-rotating screws. An example of a B anbury" mixer is the F-Seri.es Baabur/'' mixer, manufactured by Parrel. An example of a twin-screw extruder is the WP .ZSK 50 MEGAconipunderiM, manufactured by Kxupp Werner & Pfleiderer. Alter compounding, the scented resin can be added to the fibrous materia! and extruded or molded. Alternatively, master batches of fragrance- filled resins are available commercially ϊroni international Flavors and Fragrances, under the iradename Poiy!ffi M or ixom the RTP Company, in. some embodiments, the amount of fragrance in the composite is between abσus. 0.005 % by weight and about 10 % by weight, e.g., between about 0.1 % and about 5 % or 0.25 % and about 2.5 %.
Other natural wood fragrances include evergreen or redwood. Other fragrances include peppermint, cherry, strawberry, peach, lime, spearmint, cinnamon, anise, basil, bergamot, black pepper, camphor, chamomile, citronella, eucalyptus, pine, fir, geranium, ginger, grapefruit, jasmine, juniperberry, lavender, lemon, mandarin, marjoram, musk, myrhb, orange, patchouli, rose, rosemary, sage, sandalwood, tea tree, thyme, vvmtergreen, ykng yiang, vanilla, new car or mixtures of these fragrances. hi some embodiments, the amount of .fragrance in. the fibrous material-fragrance combination is between about 0.005 % by weight and about 20 % by weight, e.g., between about 0.1 % and about 5 % or 0.25 % and aboiit 2.5 %, Even other fragrances and methods are described U.S. Provisional
Application Serial No. 60/688,002, filed June ?, 2005, the entire disclosure of which is hereby incorporated by reference herein.
Any ϋf the fibrous material described above, e.g., the first 12 or second fibrous materia! 14, together with a resin, can be used to form articles such as pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, hinders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes, crutches, insulation, thread, cloth, novelties, house wares and structures. The fibrous material may be dyed before combining with the resin ami compounding to form the composites described above. In some embodiments, this dyeing can be helpful in .masking or biding the fibrous material, especially large agglomerations of the fibrous material, in molded or extruded parts. Such large agglomerations, when present in relatively high concentrations, can show up as speckles in the surfaces of the molded or extruded parts.
For example, the desired fibrous material can he dyed using an acid dye, direct dye or a reactive dye. Such dyes are available from Spectra Dyes, Keamy, NJ or Keystone Aniline Corporation, Chicago, IL. Specific examples of dyes include SPECTRA™ LIGHT YBLLOW 2G, SPECTRAC1D™ YELLOW 4GL CONC 2C)O5 SPECTRANYL™ R]-K)DAMIN E S, S PECTRAN YL™ NEUTRAL RED B5 SPECTRAMINE™ BENZOPERPURrNE5 S PECTRAD IAZ0™ BLACK OB, SPECTRAMΪN£ΪM TURQUOISE G, arid SPECTRAMΪNE™ GRBY LVL 200%, each being available from Spectra Dyes,
In same embodiments, resin color concentrates containing pigments are blended with dyes. When such blends are then compounded with the desired fibrous materia!, the fibrous material may be dyed in-situ during the compounding. Color concentrates are available from €kriant.
EXAMPLES Scanning electron micrographs were obtained on a JEOL 65C)C)O field emission scanning electron microscope. Fiber lengths and widths (i.e., diameters) were determined by Integrated Paper Sen-ices, Inc., Appletoa, WI, using an automated analyzer (TAPPI T 271 ), BET surface area was determined by Mieromerities Analytical Services, as were porosity and bulk density.
Exajngky ~ Frc^a^
A 1500 pound skid of virgin, half-gallon juice cartons made of un-priπted polycoaied white Kraft board having a bulk density of 20 Ih /W was obtained from International Paper. The material was cut into pieces 8 i/4 inches by 1 ! inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30, Model SC3G is equipped with four rotary blades, four fixed blades, and a discharge screen having IΛS inch openings. The gap between the rotary and fixed blades was set to approximately 0,020 inch. The rotary knife cutter sheared the confetti -like pieces across the knife-edges, tearing the pieces apart and releasing a fibrous material at a rate of about one pound per hour. The iibrous material had a BET surface area of 0,9748 nr/g +/- 0.0167 rsr/g, a porosity of $9.0437 percent, and a bulk density (@0.53 psia) of 0.1260 g/rnL, An average length of the fibers was 1.141 mm and an average width of the fibers was 0.027 ram, giving an average 1./D of 42; i . Scanning electron micrographs of the fibrous material are shown in Figs, 1 1 and 12 at 25 X magnification and 1000 X magnification, respectively.
Example 2 - Preparation Of Fibrous Material From Bleached Kraft Board
A 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft' was obtained from International Paper, The materia! was cut into pieces 8 1/4 inches by 1 ! inches using a guillotine cutter and fed to a Munson rotary knife cutler, Model SC30. The discharge screen had 1/8 inch openings. The gap between the rotary and fixed blades was set to approximately 0.020 inch. The rotary knife cutter sheared the confetti -like pieces, releasing a fibrous material at a rate of about one pound per hour. The fibrous material had a BET surface area of i , i 316 trf Vg -*/- 0.0103 m'V'g, a porosity of 88.3285 percent and a bulk density (@0.53 psia) of 0.1497 g/mL. Art average length of the fibers was 1 .063 mm and an average width of the fibers was 0,0245 mm. giving an average L/D of 43:1. Scanning electron micrographs of the fibrous material are shown m Figs. 13 and 14 at 25 X inagni fieation and 1000 X magnification, respectively.
0?y8£ild*ULzJb532^^
A 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lbfff was obtained from International Paper, The material was cut into pieces 8 J/4 inches by 11 inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30. The discharge screen had 1/16 inch openings. The gap between the rotary and fixed blades was set to approximately 0,020 inch. The rotary knife cutter the confetti-like pieces, releasing a fibrous material at a rate of about one pound per hour. The material resulting from the first shearing was fed back into the same setup described above aad sheared again. The resulting fibrous materia! had a BET surface area of 1 ,44OS mz/g -h1- 0.0156 in"/g, a porosity of 90,8998 percent and a hulk density (@0.53 psia) of 0.1298 g/mL. An average length of the fibers was 0.891 mm and aø average width of the fibers was 0.026 mm, giving an average L/D of 34:1. Scanning electron micrographs of the fibrous material are shown in Figs. 15 and 16 at 25 X magnification and 1000 X magnification, respectively.
Example 4 - Preparation Of Thrice Sheared Fibrous Material From Bleacheα.Kraft Board
A 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 Ib/ft* was obtained from International .Paper. The materia! was cut into pieces B 1 /4 inches by 1 1 inches using a guillotine cutter and fed to a Munsoπ rotary knife cutler. Model SC30. The discharge screen had 1/8 inch openings. The gap between the rotary and fixed blades was set io approximately 0.020 inch. The rotary knife cutter sheared the confetti -like pieces across the knife-edges. The material resulting from the first shearing was fed back into the same setup and the screen was replaced with a ϊ/16 inch screen. This material was sheared. The material resulting from the second shearing was fed back into the same setup and the screen was replaced with a 1/32 inch screen. This material was sheared. The resulting fibrous materia! had a BET surface area of 1.689? nVϊg H-/- 0.0155 πvVg, a porosity of 87.7163 percent and a balk density (@0.53 psia) of 0.1448 g/mL, An average length of the fibers was 0,824 mm and an average width of the fibers was 0,0262.mm, giving &Ώ average I../D of 32; 1. Scanning electron micrographs of the fibrous materia! are shown in Figs. 1 ? and 1 8 at 25 X magnification and ICK)O X magnification, respectively,
OTHER COMPOSITIONS AND USES OF TBE FIBROUS MATERiALS
Compositions can be prepared that include any of the fibrous materials described herein, including any of the fibrous materials, resins, additives or oilier components disclosed in U.S. Patent Nos. 6,448,307, 6,258,876, 6.207,729, 5,973,035 ami 5,952,105).
For example, any of the fibrous materials described herein can be combined wiih a solid, a liquid or a gas, e.g., a chemical or chemical formulation (m the solid or liquid stale), such as a pharmaceutical (e.g., an antibiotic), an agricultural material (e.g., plant seeds, a fertilizer, herbicide or pesticide), or ars enzyme or a formulation that includes enzymes. Compositions that include one or more type of bacteria or bacteria m combination with one or more enzymes can also be prepared.
IS Such compositions can take advantage of the fibrous material's desirable properties. For example, any of the fibrous materials can be used to absorb chemicals, potentially absorbing many times their own weight. For example, the fibrous materials can be used to absorb spilled oil, or other chemicals. Combining these fibrous materials with a microorganism, such as a bacterium, that can metabolize the oil or chemical can aid in cleanup. For example, the fibrous materials can be combined with solutions of enzymes, dried, and then used in pet bedding, or combined with a pharmaceutical and used for delivering a therapeutic agent, such as a drug. If desired, the fibrous materials can be combined with a degradabie polymer, e.g., polyglyeolic acid, polylactic acid ami copolymers of glyeoiic and lactic acid. Other degradabie materials that can be used have been discussed above,
Compositions that include fibrous materials, e.g., celluiosie or Ugnoeeilulosie materials and, e.g., chemicals or chemical formulations in the solid, liquid or gaseous slate, can be prepared, e.g., in various immersion, spraying, or blending apparatuses. For example, the compositions can be prepared using ribbon blenders, cone blenders, double cone blenders, and Patterson-Kelly "V" blenders. if desired, ϋgnin can be removed from any of the fibrous materials feat include lignin, such as Hgnocellalosic materials. Also, if desired, the fibrous materia! can. be sterilized to kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation. The fibrous materials can also be sterilized by healing the fibrous material under conditions and for a sufficient time to kill any microorganisms, or by employing a chemical sterilaπt, such as bleach (e.g., sodium hypochlorite), chlorhexidine, or ethylene oxide. Any of the fibrous materials can be washed, e.g., with a liquid such as water, to remove imy undesirable impurities and/or contaminants.
In a specific application, the fibrous materials cat) be used as a feedstock for various microorganisms, such as yeast and bacteria, that can ferment or otherwise work on the fibrous mateπais to produce a useful materia!, such as a fuel, e,g,, an alcohol, an organic acid, a hydrocarbon or hydrogen, or a protein.
The alcohol produced can be a monohydroxy alcohol e.g., ethanol. or a polyhydroxy alcohol, e.g., ethylene glycol or glycerin. Examples of alcohols that can be produced include methanol, ethanol ,. propanoi, isopropanol, butatioK ethylene glycol,
Ϊ 9 propylene glycol, ! , 4-butane diol, glycerin or mixtures of these alcohols. The organic aciά produced can a monocarboxylic acid or a polycarboxylie acid. Examples of organic acids include formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproie, palmitic acid, stearic acid, oxalic acid, rnakmic acid, succinic acid, giutaric acid, oleic acid, iiαoleie acid, glycolic acid, lactic acid, γ~hydroxybutyric acid or mixtures of these acids. The hydrocarbon produced can be, e,g., an alkane or an. aikene. Examples of hydrocarbons thai can be produced include methane, ethane, propane, isobntene, pentane, n-hexane or mixtures of these hydrocarbons.
In a particular embodiment, a fiber source that includes a eellulosie and/or iignoceliulυsic iiber source is sheared to provide a first fibrous material. The first fibrous material is then passed through a first screen having an average opening size of about 1.59 mm or less (1/16 inch, 0.0625 inch) to provide a second fibrous material. The second fibrous material is combined with a bacterium and/or enzyme, in this particular embodiment, the bacterium and/or enzyme is capable of utilizing {he second librous materia! directly without pre-treatraent to produce a fuel that includes hydrogen, an. alcohol, an organic acid and/or a hydrocarbon. hi some embodiments, prior to combining the bacteria and/or enzyme, the fibrous material is sterilized to kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation. The microorganisms can also be killed using chemical steriianls, such as bleach (e.g., sodium hypochlorite), ehlorhexidine, or ethylene oxide. hi a particular embodiment the cellulosic and/or KgnoceHuϊosic material ofthe fibrous material is Erst broken, down into lower molecular weight sugars, which are then added to a solution of yeast and/or bacteria that ferment the lower molecular weight sugars to produce ethatio!. The cellulosic and/or lignocellυlosic material can be broken down using chemicals, such as acids or bases, by enzymes, or by a combination of the two. Chemical hydrolysis of cellulosic materials is described by Bjerre, in BiotechnoL Bioeng,, 49:568 (1996) and Kim in Biotechnal. Prog,, 18:489 (2002), which are each hereby incorporated by reference herein in their entirety,
Bioethanoi strategies are discussed by DiPardo m Journal of Quthok for Biomass E i Hanoi Production ami Demand (EIA Forecasts}, 2002; Siieεhan in Biotechnology Progress, 13:8179, 1999; Martin i.n Enzyme. Microbes Technology, 31 :274, 2002; Greεr iα BioCycie, 61-65, April 2005; LyM in Microbiology and Molecular Biology Reviews, 66:3, 506-577, 2002; Ljungdahl el a!, in U.S. Patent No. 4,292,406; and Bellamy in U.S. Patent No. 4,094,742, which are each hereby incorporated by reference herein in their entirety.
Referring now to Fig. 19, a fibrous material having a low hulk density can be combined with a microorganism, e.g., freeze-dried yeast or bacteria, and/or a enzyme, and then revertibly densifϊed to a fibrous material composition having a higher bulk density. For example, a fibrous material composition having a bulk density of 0.05 g/ cm* can be dcπsified by sealing the fibrous material in a relatively gas impermeable structure, e.g., a bag made of polyethylene or a bag made of alternating layers of polyethylene and a nylon, and then evacuating the entrapped gas, e.g., air, from the structure. After evacuation of the air from the structure, the fibrous material can have, e.g., a bulk density of greater than 0.3 g/cπv\ e.g., 0.5 g/cnV, 0.6 g/enr\ 0.7 g/cmJ or more, e.g., 0.85 g/ crsr'. This can be advantageous when it is desirable to transport the fibrous material Io another location, e.g., a remote manufacturing plant, where the fibrous material composition can be added to a solution, eg,, to produce ethanol. After piercing the substantially gas impermeable structure, the densϋied fibrous material reverts to nearly its initial bulk density, e.g., greater than 60 percent of its initial bulk density, e.g., 70 percent, 80 percent. 85 percent or more, e.g., 95 percent of its initial bulk density. To reduce static electricity in. the fibrous material an anti-static agent can be added to the fibrous material. For example, a chemical anti-static compound;, e.g., a canonic compound, e.g., quaternary ammonium compound, can be added to the fibrous material
In some embodiments, the structure, e.g., bag, is formed of a material, that dissolves in a liquid, such as water. For example, the structure can be formed from a polyvinyl alcohol so that it dissolves when in contact with a wafer-based system. Such embodiments allow densifϊed structures to be added directly to solutions, e.g., that include a microorganism, without first releasing the contents of the structure, e.g.. by cutting.
OTHER EMBODIMENTS
While certain embodiments have been described, other embodiments are possible. While some embodiments use screens to provide a desired fibrous material, in some embodiments, no screens arc used to make the desired fibrous. For example, in some embodiments, a fiber source is sheared between a first pair of blades that defines a first gap, resulting in a first fibrous material. The first fibrous material is then sheared between a second pair of blades: that define a second gap that is smaller than the first gap, resulting in a second fibrous material. Similar screening processes can be repeated as many rimes as desired to produce the desired fibrous material having the desired properties.
In some embodiments, a ratio of an average length-to-diameter ratio of the first fibrous material to an average length-to-diameter of the second fibrous material is less than 1.5,
Still other embodiments are within the scope of the following claims.

Claims

WBAT 1 CLAIM IS:
1. A method of making a fuel, the method comprising: shearing a fiber source to provide a first fibrous material; passing the first fibrous material through a first screen having an average opening size of about 1.59 mm or less (1/16 inch, 0.0625 inch) to provide a second fibrous material; and combining the second fibrous material with a bacterium and/or enzyme, the bacterium and/or enzyme utilizing the second fibrous material to produce a fuel comprising hydrogen, an alcohol, an organic acid and/or a hydrocarbon-
2. The method of claim 1, wherein the alcohol is selected from the group consisting of methanol, eihanoK propanol, isopropanoi, butanol, ethylene glycol, propylene glycol 1,4-hutane diol, glycerin, and mixtures thereof,
3. The method of claim 1, wherein the organic acid is selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, valeric acid, eaproic, palmitic acid, stearic acid, oxalic acid, malonic acid, succinic acid, giυUsric acid, oleic acid, imoleie acid, glycolic acid, lactic acid, γ-hydroxybutyric acid and mixtures thereof.
4. The method of claim 1, wherein the hydrocarbon is selected from the group consisting of methane, ethane, propane, isobutene, peatane, n-hexaae, and mixtures thereof.
5. The method of claim ! , wherein the second fibrous materia! has a BET' surface area of greater than about 0.25 trT/g.
6. The method of claim 1, wherein the second fibrous materia! has a BET surface area of greater than about 1.25 m'7g.
7. The method of claim 1, wherein the second fibrous material has a porosity of greater than abfjui 85 percent,
8. A method of making a fuel, the method comprising; shearing a fiber source Io provide a first fibrous material; and passing the first fibrous materia! through a first screen having an average opening size of about 1.59 mm or less (1/16 inch. 0.0625 inch) to provide a second fibrous material; hydrolyzing the second fibrous material to provide a hydrαlyzed material; and combining the hydxolyz.ed material with bacterium and/or enzyme, the bacterium and/or enzyme- utilizing the hydrolyzed material to produce a fuel eomprismg hydrogen, an alcohol, an organic acid and/or a hydrocarbon.
9. A method of densϊfyϊng a fibrous composition, the method comprising: shearing a liber source to provide a fibrous mateπak combining the fibrous material with a bacterium and/or enzyme to provide a fibrous material composition; encapsulating the composition in a substantially gas impermeable material; and removing estopped gas from the encapsulated composition to density the composition.
10, The method of claim 9, wherein the substantially gas impermeable material is soluble in vvater.
1 L The method of claim 10, wherein the substantially gas impermeable material is in the form of a bag,
12, 'The method of claim 9, wherein after removing entrapped gas, the fibrous material has a bulk density of greater than about 0.6 e/cπr.
PCT/US2007/070972 2006-06-15 2007-06-12 Fibrous materials and compositions WO2007146922A2 (en)

Priority Applications (21)

Application Number Priority Date Filing Date Title
PL16189685T PL3135379T3 (en) 2006-06-15 2007-06-12 Methods of making a fuel
EP16189685.7A EP3135379B1 (en) 2006-06-15 2007-06-12 Methods of making a fuel
DK07798424.3T DK2032261T3 (en) 2006-06-15 2007-06-12 Process for the preparation of a fuel
KR1020097000485A KR101159628B1 (en) 2006-06-15 2007-06-12 Fibrous materials and compositions
BRPI0713417-7A BRPI0713417B1 (en) 2006-06-15 2007-06-12 METHOD FOR MANUFACTURING A FUEL
CA2655111A CA2655111C (en) 2006-06-15 2007-06-12 Fibrous materials and compositions
EP07798424.3A EP2032261B1 (en) 2006-06-15 2007-06-12 Methods of making a fuel
PL07798424T PL2032261T3 (en) 2006-06-15 2007-06-12 Methods of making a fuel
SI200731733A SI2032261T1 (en) 2006-06-15 2007-06-12 Methods of making a fuel
AP2008004725A AP2464A (en) 2006-06-15 2007-06-12 Fibrous materials and compositions
BR122017001646A BR122017001646B1 (en) 2006-06-15 2007-06-12 method for densifying a fibrous composition
EA200970015A EA013498B1 (en) 2006-06-15 2007-06-12 Fibrous materials and compositions
AU2007257741A AU2007257741B2 (en) 2006-06-15 2007-06-12 Fibrous materials and compositions
MX2008016029A MX2008016029A (en) 2006-06-15 2007-06-12 Fibrous materials and compositions.
ES07798424.3T ES2558308T3 (en) 2006-06-15 2007-06-12 Methods of obtaining a fuel
MX2012012922A MX342620B (en) 2006-06-15 2007-06-12 Fibrous materials and compositions.
EP18213457.7A EP3492173A3 (en) 2006-06-15 2007-06-12 Fibrous materials and compositions
BR122018075069-3A BR122018075069B1 (en) 2006-06-15 2007-06-12 METHOD FOR MAKING DENSER FIBER COMPOSITION
IL195910A IL195910A (en) 2006-06-15 2008-12-11 Fibrous materials and composites
IL228130A IL228130A (en) 2006-06-15 2013-08-27 Method for making a fuel from fibrous materials
IL228131A IL228131A (en) 2006-06-15 2013-08-27 Fibrous materials and compositions

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11/453,951 US7708214B2 (en) 2005-08-24 2006-06-15 Fibrous materials and composites
US11/453,951 2006-06-15

Publications (2)

Publication Number Publication Date
WO2007146922A2 true WO2007146922A2 (en) 2007-12-21
WO2007146922A3 WO2007146922A3 (en) 2009-02-26

Family

ID=38832774

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2007/070972 WO2007146922A2 (en) 2006-06-15 2007-06-12 Fibrous materials and compositions

Country Status (24)

Country Link
US (6) US7708214B2 (en)
EP (4) EP3492173A3 (en)
KR (1) KR101159628B1 (en)
CN (2) CN101541432A (en)
AP (1) AP2464A (en)
AU (1) AU2007257741B2 (en)
BR (3) BR122017001646B1 (en)
CA (1) CA2655111C (en)
DK (2) DK2032261T3 (en)
EA (1) EA013498B1 (en)
ES (2) ES2558308T3 (en)
HU (2) HUE028695T2 (en)
IL (3) IL195910A (en)
LT (1) LT3012025T (en)
MX (2) MX2008016029A (en)
MY (3) MY159433A (en)
NZ (3) NZ609636A (en)
PL (3) PL2032261T3 (en)
RU (1) RU2434945C2 (en)
SI (2) SI2032261T1 (en)
TR (1) TR201807349T4 (en)
UA (1) UA93719C2 (en)
WO (1) WO2007146922A2 (en)
ZA (1) ZA200900054B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8329455B2 (en) 2011-07-08 2012-12-11 Aikan North America, Inc. Systems and methods for digestion of solid waste
US11015059B2 (en) 2019-05-23 2021-05-25 Bolt Threads, Inc. Composite material, and methods for production thereof

Families Citing this family (74)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7537826B2 (en) * 1999-06-22 2009-05-26 Xyleco, Inc. Cellulosic and lignocellulosic materials and compositions and composites made therefrom
US7708214B2 (en) * 2005-08-24 2010-05-04 Xyleco, Inc. Fibrous materials and composites
US20150328347A1 (en) 2005-03-24 2015-11-19 Xyleco, Inc. Fibrous materials and composites
EP2564931B1 (en) * 2005-03-24 2014-08-06 Xyleco, Inc. Methods of making fibrous materials
EA025362B1 (en) 2006-10-26 2016-12-30 Ксилеко, Инк. Processing biomass
US7867358B2 (en) 2008-04-30 2011-01-11 Xyleco, Inc. Paper products and methods and systems for manufacturing such products
US8236535B2 (en) 2008-04-30 2012-08-07 Xyleco, Inc. Processing biomass
NL1035521C2 (en) * 2008-06-03 2009-12-07 Majac B V Method for recycling used clothing and household textiles.
US7900857B2 (en) * 2008-07-17 2011-03-08 Xyleco, Inc. Cooling and processing materials
MY153759A (en) 2009-02-11 2015-03-13 Xyleco Inc Processing biomass
NZ600967A (en) 2009-02-11 2013-06-28 Xyleco Inc Saccharifying biomass
WO2010093835A2 (en) 2009-02-11 2010-08-19 Xyleco, Inc. Processing biomass
AU2013203080B9 (en) * 2009-05-20 2015-09-10 Xyleco, Inc. Processing biomass
MY158952A (en) * 2009-05-20 2016-11-30 Xyleco Inc Processing biomass
NZ596930A (en) 2009-05-20 2014-06-27 Xyleco Inc Bioprocessing
PL2432865T3 (en) 2009-05-20 2018-08-31 Xyleco Inc Processing biomass
MX2011012494A (en) 2009-05-28 2012-02-21 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same.
US9512237B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Method for inhibiting the growth of microbes with a modified cellulose fiber
US9511167B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512563B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Surface treated modified cellulose from chemical kraft fiber and methods of making and using same
US20100319865A1 (en) * 2009-06-19 2010-12-23 Weyerhaeuser Nr Company Pulp for Odor Control
DK2507023T3 (en) * 2009-12-01 2023-10-30 Vive Textile Recycling Spolka Z O O PROCEDURE FOR RECYCLING USED CLOTHING AND HOUSEHOLD TEXTILES
EA201891588A3 (en) 2010-01-20 2019-04-30 Ксилеко, Инк. DISPERSION OF INITIAL RAW MATERIALS AND MATERIAL PROCESSING
SG10201602598WA (en) 2010-01-20 2016-05-30 Xyleco Inc Method and system for saccharifying and fermenting a biomass feedstock
US9604387B2 (en) 2010-04-22 2017-03-28 Forest Concepts, LLC Comminution process to produce wood particles of uniform size and shape with disrupted grain structure from veneer
US8734947B2 (en) * 2010-04-22 2014-05-27 Forst Concepts, LLC Multipass comminution process to produce precision wood particles of uniform size and shape with disrupted grain structure from wood chips
US8871346B2 (en) 2010-04-22 2014-10-28 Forest Concepts, LLC Precision wood particle feedstocks with retained moisture contents of greater than 30% dry basis
US8497019B2 (en) 2010-04-22 2013-07-30 Forest Concepts, LLC Engineered plant biomass particles coated with bioactive agents
US8497020B2 (en) 2010-04-22 2013-07-30 Forest Concepts, LLC Precision wood particle feedstocks
US8507093B2 (en) * 2010-04-22 2013-08-13 Forest Concepts, LLC Comminution process to produce precision wood particles of uniform size and shape with disrupted grain structure from wood chips
US9005758B2 (en) 2010-04-22 2015-04-14 Forest Concepts, LLC Multipass rotary shear comminution process to produce corn stover particles
US8481160B2 (en) 2010-04-22 2013-07-09 Forest Concepts, LLC Bimodal and multimodal plant biomass particle mixtures
US9061286B2 (en) 2010-04-22 2015-06-23 Forest Concepts, LLC Comminution process to produce precision wood particles of uniform size and shape with disrupted grain structure from wood chips
US8034449B1 (en) * 2010-04-22 2011-10-11 Forest Concepts, LLC Engineered plant biomass feedstock particles
US8758895B2 (en) 2010-04-22 2014-06-24 Forest Concepts, LLC Engineered plant biomass particles coated with biological agents
US9440237B2 (en) * 2010-04-22 2016-09-13 Forest Concepts, LLC Corn stover biomass feedstocks with uniform particle size distribution profiles at retained field moisture contents
AU2011279924B2 (en) 2010-07-19 2015-01-29 Xyleco, Inc. Processing biomass
US8651403B2 (en) * 2010-07-21 2014-02-18 E I Du Pont De Nemours And Company Anhydrous ammonia treatment for improved milling of biomass
US20120024859A1 (en) * 2010-07-30 2012-02-02 Francesco Longoni Container
CN102478716B (en) * 2010-11-30 2013-08-28 东莞冠狄塑胶有限公司 Manufacturing method of glasses rack sheet material
US8722773B2 (en) 2011-02-14 2014-05-13 Weyerhaeuser Nr Company Polymeric composites
US8757092B2 (en) 2011-03-22 2014-06-24 Eco-Composites Llc Animal bedding and associated method for preparing the same
US9737047B2 (en) * 2011-03-22 2017-08-22 Ccd Holdings Llc Method for the treatment, control, minimization, and prevention of bovine mastitis
US8765010B2 (en) 2011-03-22 2014-07-01 Eco-Composites Llc Lignocellulosic fibrous composites and associated methods for preparing the same
US9181134B1 (en) 2011-04-27 2015-11-10 Israzion Ltd. Process of converting textile solid waste into graphite simple or complex shaped manufacture
AU2012268700B2 (en) 2011-05-23 2017-02-02 Gp Cellulose Gmbh Softwood kraft fiber having improved whiteness and brightness and methods of making and using the same
FI124380B (en) * 2011-11-15 2014-07-31 Upm Kymmene Corp Composite product, method of manufacture of a composite product and its use, and final product
TWI628331B (en) 2012-01-12 2018-07-01 Gp纖維股份有限公司 A low viscosity kraft fiber having reduced yellowing properties and methods of making and using the same
US9328231B2 (en) * 2012-02-14 2016-05-03 Weyerhaeuser Nr Company Composite polymer
JP6242859B2 (en) 2012-04-18 2017-12-06 ゲーペー ツェルローゼ ゲーエムベーハー Use of surfactants to treat pulp and improve kraft pulp incorporation into fibers for the production of viscose and other secondary fiber products
UA116630C2 (en) 2012-07-03 2018-04-25 Ксілеко, Інк. METHOD OF CONVERTING SUGAR TO FURFURYL ALCOHOL
EP2890539B1 (en) 2012-08-28 2018-10-31 UPM-Kymmene Corporation Method for manufacturing a composite product, and composite product so produced
PL2708643T3 (en) * 2012-09-14 2018-10-31 Mediterranea Solutions S.U.A.R.L. Method for pretreating biomasses prior to conversion to biofuel
JP5948222B2 (en) * 2012-11-02 2016-07-06 ユニ・チャーム株式会社 Separation apparatus and separation method for material related to absorbent article
US9682488B2 (en) * 2013-01-15 2017-06-20 Barry Beyerlein Double-barrel trimmer for plant materials
EP2954115B1 (en) 2013-02-08 2022-01-12 GP Cellulose GmbH Softwood kraft fiber having an improved a-cellulose content and its use in the production of chemical cellulose products
US10138598B2 (en) 2013-03-14 2018-11-27 Gp Cellulose Gmbh Method of making a highly functional, low viscosity kraft fiber using an acidic bleaching sequence and a fiber made by the process
EP2971338A2 (en) 2013-03-15 2016-01-20 GP Cellulose GmbH A low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US9650489B2 (en) * 2013-09-27 2017-05-16 Toyo Seikan Group Holdings, Ltd. Method for degrading biodegradable resin
JP5977726B2 (en) * 2013-11-07 2016-08-24 鈴鹿エンヂニヤリング株式会社 Rubber bale shredding method and apparatus
US10227623B2 (en) 2013-11-24 2019-03-12 E I Du Pont De Nemours And Company High force and high stress destructuring of cellulosic biomass
DE202014001280U1 (en) * 2014-02-11 2014-04-04 Landpack GmbH & Co. KG Insulated packaging for thermal insulation or shock absorption from straw or hay
US9809011B1 (en) 2014-06-11 2017-11-07 Giuseppe Puppin Composite fabric member and methods
DE102014225105B4 (en) * 2014-12-08 2019-01-03 Currenta Gmbh & Co.Ohg Process for the mechanical treatment of carbon fibers
US10456959B2 (en) * 2015-01-21 2019-10-29 TieBam, Inc. Bamboo railroad tie manufacturing system
ITUA20164301A1 (en) * 2016-05-24 2017-11-24 Maria Giovanna Gamberini TERMOCOMPATTATORE
US11078630B2 (en) * 2016-11-03 2021-08-03 Oregon State University Molded pomace pulp products and methods
CA3040734A1 (en) 2016-11-16 2018-05-24 Gp Cellulose Gmbh Modified cellulose from chemical fiber and methods of making and using the same
WO2019050960A1 (en) 2017-09-05 2019-03-14 Poet Research, Inc. Methods and systems for propagation of a microorganism using a pulp mill and/or a paper mill waste by-product, and related methods and systems
CA3080669A1 (en) 2017-10-27 2019-05-02 Xyleco, Inc. Processing biomass
US11697538B2 (en) * 2018-06-21 2023-07-11 First Quality Tissue, Llc Bundled product and system and method for forming the same
US11738927B2 (en) * 2018-06-21 2023-08-29 First Quality Tissue, Llc Bundled product and system and method for forming the same
CN114102789B (en) * 2021-11-12 2023-04-07 浙江品阁木业有限公司 Dewatering device of modified fiberboard raw material
CN114957964B (en) * 2022-06-17 2023-03-31 宋伟杰 Degradable automobile foot mat material and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4237226A (en) 1979-02-23 1980-12-02 Trustees Of Dartmouth College Process for pretreating cellulosic substrates and for producing sugar therefrom
US5705369A (en) 1994-12-27 1998-01-06 Midwest Research Institute Prehydrolysis of lignocellulose
US7901511B2 (en) 2001-02-28 2011-03-08 Iogen Energy Corporation Method of processing lignocellulosic feedstock for enhanced xylose and ethanol production

Family Cites Families (361)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1824221A (en) 1928-10-24 1931-09-22 Masonite Corp Process and apparatus for disintegration of fibrous material
US2519442A (en) 1944-04-28 1950-08-22 Saint Gobain Compositions containing cellulosic filler united by polyvinyl chloride
US2516847A (en) 1944-12-01 1950-08-01 Masonite Corp Process of sizing exploded fibers
US2558378A (en) 1947-01-15 1951-06-26 Delaware Floor Products Inc Composition for floor and wall covering comprising plasticized vinyl resin and filler and method of making same
US2635976A (en) 1948-06-15 1953-04-21 Plywood Res Foundation Method of making synthetic constructional boards and products thereof
US2658828A (en) 1948-09-15 1953-11-10 Chemloch Corp Process of combining synthetic resins and other materials with cellulose
US2665261A (en) 1950-05-12 1954-01-05 Allied Chem & Dye Corp Production of articles of high impact strength
US2680102A (en) 1952-07-03 1954-06-01 Homasote Company Fire-resistant product from comminuted woody material, urea, or melamine-formaldehyde, chlorinated hydrocarbon resin, and hydrated alumina
US2757150A (en) 1953-01-30 1956-07-31 Weyerhaeuser Timber Co Preparing hot-moldable thermosetting resin and cellulose fiber mixtures
US2935763A (en) 1954-09-01 1960-05-10 Us Rubber Co Method of forming pellets of a synthetic rubber latex and a particulate resin
US2789903A (en) 1954-09-02 1957-04-23 Celanese Corp Process for production of shaped articles comprising fibrous particles and a copolymer of vinyl acetate and an ethylenically unsaturated acid
US3308218A (en) 1961-05-24 1967-03-07 Wood Conversion Co Method for producing bonded fibrous products
US3493527A (en) 1962-06-07 1970-02-03 George Berthold Edward Schuele Moldable composition formed of waste wood or the like
GB1046246A (en) 1962-06-07 1966-10-19 George Berthold Edward Schuele Improvements in or relating to the utilisation of natural fibrous materials
US3645939A (en) 1968-02-01 1972-02-29 Us Plywood Champ Papers Inc Compatibilization of hydroxyl containing materials and thermoplastic polymers
US3516953A (en) 1968-03-25 1970-06-23 Ernest Herbert Wood Granular,free-flowing,synthetic thermosetting aminoplast resin molding composition containing defiberized alpha-cellulosic pulp of a certain fiber length wherein said filler is substantially the sole filler present
US3596314A (en) 1968-11-26 1971-08-03 Hitco Apparatus for forming a densified fibrous article
US3697364A (en) 1970-04-16 1972-10-10 Monsanto Co Discontinuous cellulose reinforced elastomer
US3836412A (en) 1970-04-16 1974-09-17 Monsanto Co Preparation of discontinuous fiber reinforced elastomer
US3718536A (en) 1970-04-22 1973-02-27 Thilmany Pulp & Paper Co Composite board and method of manufacture
US3671615A (en) 1970-11-10 1972-06-20 Reynolds Metals Co Method of making a composite board product from scrap materials
US3709845A (en) 1971-07-06 1973-01-09 Monsanto Co Mixed discontinuous fiber reinforced composites
JPS5654335B2 (en) 1972-07-11 1981-12-24
SE368793B (en) 1972-11-03 1974-07-22 Sonesson Plast Ab
JPS594447B2 (en) 1972-12-28 1984-01-30 日石三菱株式会社 synthetic paper
CH570869A5 (en) 1973-03-23 1976-05-14 Icma San Giorgio S R L Ind Cos
US4305901A (en) 1973-07-23 1981-12-15 National Gypsum Company Wet extrusion of reinforced thermoplastic
SE398134B (en) 1973-11-19 1977-12-05 Sunden Olof PROCEDURE FOR MODIFICATION OF CELLULOSIAN FIBERS BY SILIC ACID AND IMPREGNATION SOLUTION FOR PERFORMANCE OF THE PROCEDURE
US4056591A (en) 1973-12-26 1977-11-01 Monsanto Company Process for controlling orientation of discontinuous fiber in a fiber-reinforced product formed by extrusion
SE7415817L (en) 1974-01-18 1975-07-21 Baehre & Greten
US3943079A (en) 1974-03-15 1976-03-09 Monsanto Company Discontinuous cellulose fiber treated with plastic polymer and lubricant
US4016232A (en) 1974-05-02 1977-04-05 Capital Wire And Cable, Division Of U.S. Industries Process of making laminated structural member
US3956541A (en) 1974-05-02 1976-05-11 Capital Wire & Cable, Division Of U. S. Industries Structural member of particulate material and method of making same
US4020212A (en) 1974-09-13 1977-04-26 Phillips Petroleum Company Polyolefin fibers useful as fiberfill treated with finishing agent comprising an organopolysiloxane and a surface active softener
US3956555A (en) 1974-09-23 1976-05-11 Potlatch Corporation Load carrying member constructed of oriented wood strands and process for making same
US4058580A (en) 1974-12-02 1977-11-15 Flanders Robert D Process for making a reinforced board from lignocellulosic particles
FR2296513A1 (en) 1974-12-31 1976-07-30 Inst Nat Rech Chimique MANUFACTURING PROCESS OF FINISHED OR SEMI-FINISHED PRODUCTS FROM MIXTURES OF WASTE OF DIFFERENT SYNTHETIC RESINS
US4097648A (en) 1975-02-10 1978-06-27 Capital Wire & Cable, Division Of U.S. Industries, Inc. Laminated structural member and method of making same
US3985927A (en) 1975-02-24 1976-10-12 Nekoosa Edwards Paper Company, Inc. Compositions and method for producing a chemical watermark on finished paper products
US4045603A (en) 1975-10-28 1977-08-30 Nora S. Smith Construction material of recycled waste thermoplastic synthetic resin and cellulose fibers
NO138127C (en) 1975-12-01 1978-07-12 Elopak As PROCEDURE FOR "MUNICIPAL" WASTE AA MANUFACTURING RAW MATERIAL FOR PRESS BODIES
DE2610721C3 (en) 1976-03-13 1978-12-21 Rehau-Plastiks Gmbh, 8673 Rehau Use of a plastic-wood flour mixture for the production of insulation material for the electrical industry
US4112038A (en) 1976-09-02 1978-09-05 Lowe Paper Company Method for producing molded articles
US4204010A (en) 1976-09-17 1980-05-20 W. R. Grace & Co. Radiation curable, ethylenically unsaturated thixotropic agent and method of preparation
DE2647944C2 (en) 1976-10-22 1979-04-12 Rolf 8502 Zirndorf Schnause Method and device for the production of moldings from thermoplastics and a sheet-shaped, chipped, fibrous, non-thermoplastic material
CA1099858A (en) 1976-11-11 1981-04-28 Heikki Mamers Recovery of fibre from laminated carton boards
US4263184A (en) 1977-01-05 1981-04-21 Wyrough And Loser, Inc. Homogeneous predispersed fiber compositions
FR2381804A1 (en) 1977-02-28 1978-09-22 Solvay MOLDABLE COMPOSITIONS BASED ON THERMOPLASTIC POLYMERS AND VEGETABLE FIBROUS MATERIALS AND USE OF THESE COMPOSITIONS FOR CALENDERING AND THERMOFORMING
US4184311A (en) * 1977-03-25 1980-01-22 Rood Leonard D Fire retardant insulation
NL184773C (en) 1977-04-19 1989-11-01 Lankhorst Touwfab Bv METHOD FOR PROCESSING THERMOPLASTIC PLASTIC MATERIAL INTO AN ARTICLE WITH THE PROCESSING AND PROCESSING PROPERTIES OF WOOD.
US4123489A (en) * 1977-05-17 1978-10-31 Flett Development Company Method for converting waste paper products into useful forms
US4145389A (en) 1977-08-22 1979-03-20 Smith Teddy V Process for making extruded panel product
US4277428A (en) 1977-09-14 1981-07-07 Masonite Corporation Post-press molding of man-made boards to produce contoured furniture parts
US4508595A (en) 1978-05-25 1985-04-02 Stein Gasland Process for manufacturing of formed products
DE2831616C2 (en) 1978-07-19 1984-08-09 Kataflox Patentverwaltungs-Gesellschaft mbH, 7500 Karlsruhe Process for producing a non-combustible molded body
US4244847A (en) 1978-08-10 1981-01-13 The Gates Rubber Company Fibrated admix or polymer and process therefore
US4202804A (en) 1978-09-11 1980-05-13 Desoto, Inc. Viscosity stable, stainable wood textured caulking composition containing water immiscible organic solvent
JPS5944963B2 (en) 1978-10-06 1984-11-02 ロンシール工業株式会社 Method for manufacturing vinyl chloride sheet with printed shibori pattern
DE2845112C3 (en) 1978-10-17 1981-11-05 Casimir Kast Gmbh & Co Kg, 7562 Gernsbach Process and plant for the production of mats from cellulosic fibers and process for the production of molded parts from these
DE7831283U1 (en) 1978-10-20 1979-04-05 Werz Furnier Sperrholz Stackable pallet with integrated stacking cam
US4248820A (en) 1978-12-21 1981-02-03 Board Of Control Of Michigan Technological University Method for molding apertures in molded wood products
US4440708A (en) 1978-12-21 1984-04-03 Board Of Control Of Michigan Technological University Method for molding articles having non-planar portions from matted wood flakes
US4303019A (en) 1979-03-07 1981-12-01 Board Of Control Of Michigan Technological University Articles molded from papermill sludge
US5628830A (en) 1979-03-23 1997-05-13 The Regents Of The University Of California Enzymatic hydrolysis of biomass material
US4311621A (en) 1979-04-26 1982-01-19 Kikkoman Corporation Process for producing a filler for adhesive for bonding wood
US4239679A (en) 1979-06-27 1980-12-16 Diamond Shamrock Corporation High bulk density rigid poly(vinyl chloride) resin powder composition and preparation thereof
US4279790A (en) 1979-07-05 1981-07-21 Kabushiki Kaisha Mikuni Seisakusho Composite material compositions using wasterpaper and method of producing same
SE8005194L (en) 1979-07-17 1981-01-18 Lion Corp THERMOPLASTIC COMPOSITION AND SET TO FORM FORM THEREOF
AU553080B2 (en) * 1979-08-10 1986-07-03 Timothy Warren Gilder Method of forming wood fibres
US4248743A (en) 1979-08-17 1981-02-03 Monsanto Company Preparing a composite of wood pulp dispersed in a polymeric matrix
WO1981000588A1 (en) 1979-08-29 1981-03-05 M Hewitt Cored plastics profiles and manufacture of frames for windows and the like therefrom
US4265846A (en) 1979-10-05 1981-05-05 Canadian Patents And Development Limited Method of binding lignocellulosic materials
US4393020A (en) 1979-12-20 1983-07-12 The Standard Oil Company Method for manufacturing a fiber-reinforced thermoplastic molded article
CA1173380A (en) 1980-02-19 1984-08-28 Michael I. Sherman Acid hydrolysis of biomass for ethanol production
US4480035A (en) 1980-06-09 1984-10-30 Sukomal Roychowdhury Production of hydrogen
FR2483966A1 (en) 1980-06-10 1981-12-11 Rhone Poulenc Textile SOLUTIONS CONFORMABLE FROM CELLULOSE MIXTURES AND VINYL POLYCHLORIDE AND FORM ARTICLES THEREOF
US4323625A (en) 1980-06-13 1982-04-06 Monsanto Company Composites of grafted olefin polymers and cellulose fibers
US4328136A (en) 1980-12-30 1982-05-04 Blount David H Process for the production of cellulose-silicate products
US4400470A (en) 1981-01-14 1983-08-23 Wisconsin Alumni Research Foundation Use of co-cultures in the production of ethanol by the fermentation of biomass
US4414267A (en) 1981-04-08 1983-11-08 Monsanto Company Method for treating discontinuous cellulose fibers characterized by specific polymer to plasticizer and polymer-plasticizer to fiber ratios, fibers thus treated and composites made from the treated fibers
US4376144A (en) 1981-04-08 1983-03-08 Monsanto Company Treated fibers and bonded composites of cellulose fibers in vinyl chloride polymer characterized by an isocyanate bonding agent
US4359534A (en) 1981-04-28 1982-11-16 The United States Of America As Represented By The Secretary Of Agriculture Conversion of D-xylose to ethanol by the yeast Pachysolen tannophilus
US4511656A (en) 1981-05-15 1985-04-16 Purdue Research Foundation Direct fermentation of D-xylose to ethanol by a xylose-fermenting yeast mutant
US4368268A (en) 1981-05-15 1983-01-11 Purdue Research Foundation Direct fermentation of D-xylose to ethanol by a xylose-fermenting yeast mutant
US4426470A (en) 1981-07-27 1984-01-17 The Dow Chemical Company Aqueous method of making reinforced composite material from latex, solid polymer and reinforcing material
HU183546B (en) 1981-08-19 1984-05-28 Muanyagipari Kutato Intezet Process for preparing a combined substance containing a thermoplastic material, a fibrous polymeric skeleton substance of natural origin and an insaturated polyester
DE3147989A1 (en) 1981-12-04 1983-06-16 Hoechst Ag, 6230 Frankfurt DECORATIVE, IN PARTICULAR PLATE-SHAPED MOLDED PART, METHOD FOR THE PRODUCTION THEREOF AND THE USE THEREOF
EP0108068B1 (en) 1981-12-11 1993-06-02 KUBAT, Josef Method to produce composites based on cellulose or lignocellulosic materials and plastics
US4382108A (en) 1981-12-21 1983-05-03 The Upjohn Company Novel compositions and process
US4738723A (en) 1981-12-24 1988-04-19 Gulf States Asphalt Co. Asbestos-free asphalt composition
CA1196461A (en) 1982-03-03 1985-11-12 Sadao Nishibori Method for manufacturing wood-like molded product
US4420351A (en) 1982-04-29 1983-12-13 Tarkett Ab Method of making decorative laminated products such as tiles, panels or webs from cellulosic materials
US4455709A (en) 1982-06-16 1984-06-26 Zanini Walter D Floor mounted guide and shim assembly for sliding doors
US4562218A (en) 1982-09-30 1985-12-31 Armstrong World Industries, Inc. Formable pulp compositions
DE3472565D1 (en) 1983-03-23 1988-08-11 Chuo Kagaku Co Production of resin foam by aqueous medium
BG39560A1 (en) 1983-08-25 1986-07-15 Natov Polyvinylchloride composition
US4520530A (en) 1983-09-02 1985-06-04 Akiva Pinto Fiber feeding apparatus with a pivoted air exhaust wall portion
DE3336647A1 (en) 1983-10-08 1985-04-25 Hoechst Ag, 6230 Frankfurt MOLDING DIMENSIONS BASED ON VINYL CHLORIDE POLYMERISATS AND METHOD FOR THE PRODUCTION OF FILMS FROM THESE SHAPING MATERIALS FOR THE PREPARATION OF COUNTERFEIT-SECURE SECURITIES
DE3346469A1 (en) 1983-12-22 1985-07-18 Heggenstaller, Anton, 8892 Kühbach METHOD AND DEVICE FOR EXTRUDING PLANT SMALL PARTS MIXED WITH BINDERS, IN PARTICULAR SMALL WOOD PARTS
US4609624A (en) 1984-02-03 1986-09-02 Les Services De Consultation D.B. Plus Limitee Process for producing isopropyl alcohol from cellulosic substrates
GB8404000D0 (en) 1984-02-15 1984-03-21 Unilever Plc Wiping surfaces
US4597928A (en) 1984-03-23 1986-07-01 Leningradsky Tekhnologichesky Institute Tselljulozno-Bumazhnoi Promyshlennosti Method for fiberboard manufacture
JPS60206604A (en) 1984-03-30 1985-10-18 Ota Shoji Conversion of lignocellulose material into recomposed compound
DE3417712A1 (en) 1984-05-12 1985-11-14 Andreas 8077 Reichertshofen Pöhl BOOK PRESS
JPS6131447A (en) 1984-07-23 1986-02-13 Kanegafuchi Chem Ind Co Ltd Thermoplastic woody composition
FR2568164B1 (en) 1984-07-27 1987-09-04 Ostermann Michel PROCESS FOR PRODUCING DECORATIVE PRODUCTS FROM FRAGMENTS OR PIECES OF WOOD AND PRODUCTS OBTAINED
US4713291A (en) 1984-09-06 1987-12-15 Mitsubishi Rayon Company Ltd. Fragrant fiber
DE3472654D1 (en) 1984-09-20 1988-08-18 Werz Pressholz Werzalit Pallet
DE3446139A1 (en) 1984-12-18 1986-06-19 Andreas Peter Dipl.-Ing. 8200 Rosenheim Pöhl POT FOR METAL COATING
US4610900A (en) 1984-12-19 1986-09-09 Sadao Nishibori Wood-like molded product of synthetic resin
JPS61151266A (en) 1984-12-25 1986-07-09 Chisso Corp Cellulosic filler for thermoplastic resin
DE3504686A1 (en) * 1985-02-12 1986-08-14 Hercules Vollkornmühlenbäckerei GmbH, 4000 Düsseldorf Process for producing a storable ready-to-use sour dough/flour mixture
DE3507640A1 (en) 1985-03-05 1986-09-11 Hubert 5778 Meschede Möller METHOD FOR PRODUCING REINFORCED PROFILE PARTS
US4812410A (en) 1985-04-12 1989-03-14 George Weston Limited Continuous process for ethanol production by bacterial fermentation
US4717742A (en) 1985-05-29 1988-01-05 Beshay Alphons D Reinforced polymer composites with wood fibers grafted with silanes - grafting of celluloses or lignocelluloses with silanes to reinforce the polymer composites
US5104411A (en) 1985-07-22 1992-04-14 Mcneil-Ppc, Inc. Freeze dried, cross-linked microfibrillated cellulose
US4911700A (en) 1985-07-22 1990-03-27 Mcneil-Ppc, Inc. Cross-linked microfibrillated cellulose prepared from pure generating particles
US4840903A (en) 1985-08-08 1989-06-20 The United States Of America As Represented By The United States Department Of Energy Process for producing ethanol from plant biomass using the fungus paecilomyces sp.
US4716062A (en) 1985-11-08 1987-12-29 Max Klein Composite materials, their preparation and articles made therefrom
US4659754A (en) 1985-11-18 1987-04-21 Polysar Limited Dispersions of fibres in rubber
US4865788A (en) 1985-12-02 1989-09-12 Sheller-Globe Corporation Method for forming fiber web for compression molding structural substrates for panels and fiber web
US4734236A (en) 1985-12-02 1988-03-29 Sheller-Globe Corporation Method for forming fiber web for compression molding structural substrates for panels
US4663225A (en) 1986-05-02 1987-05-05 Allied Corporation Fiber reinforced composites and method for their manufacture
US4833181A (en) 1986-07-25 1989-05-23 Tonen Sekiyukagaku Kabushiki Kaisha Polyolefin composition containing cellulose fibers and a deodorizer
GB8618729D0 (en) 1986-07-31 1986-09-10 Wiggins Teape Group Ltd Fibrous structure
JPH0679811B2 (en) 1986-08-06 1994-10-12 トヨタ自動車株式会社 Method for manufacturing wood-based molded body
DE3630937A1 (en) 1986-09-11 1988-03-24 Rehau Ag & Co USE OF NATURAL CELLULOSE FIBERS AS ADDITIVE TO POLYVINYL CHLORIDE
US4810445A (en) 1986-09-26 1989-03-07 Fortifiber Corporation Process for making pressboard from poly-coated paper
US4769274A (en) 1986-12-22 1988-09-06 Tarkett Inc. Relatively inexpensive thermoformable mat of reduced density and rigid laminate which incorporates the same
US4769109A (en) 1986-12-22 1988-09-06 Tarkett Inc. Relatively inexpensive thermoformable mat and rigid laminate formed therefrom
US4791020A (en) 1987-02-02 1988-12-13 Novacor Chemicals Ltd. Bonded composites of cellulose fibers polyethylene
DE3726921A1 (en) 1987-02-10 1988-08-18 Menzolit Gmbh SEMI-FINISHED PRODUCT AND METHOD AND DEVICE FOR PRODUCING MOLDED SEMI-PREPARED PRODUCTS FROM THERMOPLAST
US4818604A (en) 1987-03-27 1989-04-04 Sub-Tank Renewal Systems, Inc. Composite board and method
DE3714828A1 (en) 1987-05-01 1988-11-17 Rettenmaier Stefan METHOD FOR PRODUCING BITUMEN MASSES
US4840902A (en) 1987-05-04 1989-06-20 George Weston Limited Continuous process for ethanol production by bacterial fermentation using pH control
US4746688A (en) 1987-05-21 1988-05-24 Ford Motor Company Remoldable, wood-filled acoustic sheet
ES2027653T3 (en) 1987-05-23 1992-06-16 Mario Miani METHOD OF MANUFACTURING PANELS, APPARATUS TO MAKE THIS METHOD AND PANELS OBTAINED WITH THEM.
DE3718545A1 (en) 1987-06-03 1988-12-22 Signode System Gmbh EDGE PROTECTION PROFILE SECTION AND METHOD FOR PRODUCING THE SAME
DE3725965A1 (en) 1987-08-05 1989-02-16 Signode System Gmbh METHOD FOR PRODUCING MOLDED BODIES FROM PAPER AND A THERMOPLASTIC PLASTIC
FR2622833B1 (en) 1987-11-06 1990-04-27 Omnium Traitement Valorisa PROCESS AND INSTALLATION FOR THE MANUFACTURE OF MOLDED OR EXTRUDED OBJECTS FROM WASTE CONTAINING PLASTIC MATERIALS
CN1017881B (en) 1987-12-16 1992-08-19 库特·赫尔德·法布里肯特 Apparatus and method for manufacturing wood plank
BR8807863A (en) 1987-12-22 1990-10-09 Willem Hemmo Kampen PROCESS AND APPARATUS FOR THE PRODUCTION OF ETHANOL, GLYCER, SUCCINIC ACID AND DRY GRAINS OF FLUID FREELY AND SOLUBLE ELEMENTS
FR2625645B1 (en) 1988-01-13 1991-07-05 Wogegal Sa PROCESS AND INSTALLATION FOR PRODUCING A PRODUCT AS A CULTURE SUPPORT
US4854204A (en) 1988-03-03 1989-08-08 Am International Incorporated Rotary knife paper trimmer with long life shearing surfaces for trimming thick and shingled paper products
US5183837A (en) 1988-03-30 1993-02-02 Presidenza Del Consiglio Dei Ministri - Ufficio Del Ministro Per Il Coordinamento Delle Iniziativae Per La Ricerca Scientifica E Tecnologica Process for binding cellulosic materials with a binding agent of an aqueous emulsions of polyisocyanates and cellulose ether
US4927579A (en) 1988-04-08 1990-05-22 The Dow Chemical Company Method for making fiber-reinforced plastics
US5424202A (en) 1988-08-31 1995-06-13 The University Of Florida Ethanol production by recombinant hosts
US5554520A (en) 1988-08-31 1996-09-10 Bioenergy International, L.C. Ethanol production by recombinant hosts
US5028539A (en) 1988-08-31 1991-07-02 The University Of Florida Ethanol production using engineered mutant E. coli
US5487989A (en) 1988-08-31 1996-01-30 Bioenergy International, L.C. Ethanol production by recombinant hosts
US4963603A (en) 1989-05-24 1990-10-16 Armstrong World Industries, Inc. Composite fiberboard and process of manufacture
DE3841310C1 (en) 1988-12-08 1990-06-07 Werzalit Ag + Co, 7141 Oberstenfeld, De
DE3842072C1 (en) 1988-12-14 1989-12-28 Pallmann Maschinenfabrik Gmbh & Co Kg, 6660 Zweibruecken, De
US5582682A (en) 1988-12-28 1996-12-10 Ferretti; Arthur Process and a composition for making cellulosic composites
AU623471B2 (en) 1989-01-09 1992-05-14 Peter T. Locke A composite board and method of producing same
US4929498A (en) 1989-01-31 1990-05-29 James River Corporation Of Virginia Engineered-pulp wet wiper fabric
DE3903022C1 (en) 1989-02-02 1990-04-26 Hermann Berstorff Maschinenbau Gmbh, 3000 Hannover, De
US4973440A (en) 1989-03-15 1990-11-27 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method for production of fiber-reinforced thermosetting resin molding material
US5093058A (en) 1989-03-20 1992-03-03 Medite Corporation Apparatus and method of manufacturing synthetic boards
US5432000A (en) 1989-03-20 1995-07-11 Weyerhaeuser Company Binder coated discontinuous fibers with adhered particulate materials
US5230959A (en) 1989-03-20 1993-07-27 Weyerhaeuser Company Coated fiber product with adhered super absorbent particles
US5498478A (en) 1989-03-20 1996-03-12 Weyerhaeuser Company Polyethylene glycol as a binder material for fibers
CA1332987C (en) 1989-04-19 1994-11-08 Govinda Raj Process for chemical treatment of discontinuous cellulosic fibers and composites of polyethylene and treated fibers
US5008310A (en) 1989-05-15 1991-04-16 Beshay Alphons D Polymer composites based cellulose-V
US5076503A (en) * 1989-07-12 1991-12-31 Cook Robert L Size reduction processing apparatus for solid material
CA2014089C (en) 1989-07-21 1997-01-14 Vernon L. Lamb Apparatus and method for making pressboard from poly-coated paper using relative movement of facing webs
BR9007558A (en) 1989-07-24 1992-06-23 A C I Int Ltd PERFECTED LAMINATED MATERIAL AND PROCESS FOR ITS PRODUCTION
US5075359A (en) 1989-10-16 1991-12-24 Ici Americas Inc. Polymer additive concentrate
DE69016194T2 (en) 1989-11-16 1995-05-24 Mitsui Petrochemical Ind RESIN MIXTURE FOR FILMS AND METHOD FOR PRODUCING FILMS USING THE RESIN MIXTURE.
US5002713A (en) 1989-12-22 1991-03-26 Board Of Control Of Michigan Technological University Method for compression molding articles from lignocellulosic materials
US7109005B2 (en) 1990-01-15 2006-09-19 Danisco Sweeteners Oy Process for the simultaneous production of xylitol and ethanol
FI86440C (en) 1990-01-15 1992-08-25 Cultor Oy FRAME FOR SAMPLING OF XYLITOL OR ETHANOL.
US5124519A (en) 1990-01-23 1992-06-23 International Paper Company Absorbent microwave susceptor composite and related method of manufacture
US5064692A (en) 1990-02-15 1991-11-12 International Paper Company Method for producing paper products having increased gloss in which surface characteristics of a release film are imparted to coated substrates
US5082605A (en) 1990-03-14 1992-01-21 Advanced Environmental Recycling Technologies, Inc. Method for making composite material
US5096406A (en) 1990-03-14 1992-03-17 Advanced Environmental Recycling Technologies, Inc. Extruder assembly for composite materials
US5096046A (en) 1990-03-14 1992-03-17 Advanced Environmental Recycling Technologies, Inc. System and process for making synthetic wood products from recycled materials
US5088910A (en) 1990-03-14 1992-02-18 Advanced Environmental Recycling Technologies, Inc. System for making synthetic wood products from recycled materials
US5213021A (en) 1990-03-14 1993-05-25 Advanced Environmental Recycling Technologies, Inc. Reciprocating cutter assembly
US5759680A (en) 1990-03-14 1998-06-02 Advanced Environmetal Recycling Technologies, Inc. Extruded composite profile
US5084135A (en) 1990-03-27 1992-01-28 Advanced Environmental Recycling Technologies, Inc. Recycling plastic coated paper product waste
US5268074A (en) 1990-03-27 1993-12-07 Advanced Environmental Recycling Technologies, Inc. Method for recycling polymeric film
US5100603A (en) 1990-04-30 1992-03-31 Neefe Charles W Method of recycling multimaterial containers
EP0510228B1 (en) * 1990-05-23 1997-01-22 Didier-Werke Ag Method and apparatus for opening of a fiber agglomerate
US5134023A (en) 1990-07-05 1992-07-28 Forintek Canada Corp. Process for making stable fiberboard from used paper and fiberboard made by such process
US5100545A (en) 1990-12-03 1992-03-31 Advanced Environmental Recycling Technologies, Inc. Separation tank
DE4042222A1 (en) 1990-12-29 1992-07-02 Pwa Industriepapier Gmbh METHOD FOR REPROCESSING THERMOPLAST COATED PACKAGING MATERIALS AND THERMOPLASTIC MATERIAL FOR FURTHER PROCESSING
US5075057A (en) 1991-01-08 1991-12-24 Hoedl Herbert K Manufacture of molded composite products from scrap plastics
US5100791A (en) 1991-01-16 1992-03-31 The United States Of America As Represented By The United States Department Of Energy Simultaneous saccharification and fermentation (SSF) using cellobiose fermenting yeast Brettanomyces custersii
US5134944A (en) 1991-02-28 1992-08-04 Keller Leonard J Processes and means for waste resources utilization
WO1992016686A1 (en) 1991-03-21 1992-10-01 Advanced Recycling Technologies, Inc. Method for recycling plastic coated paper product waste and polymeric film
US5372939A (en) 1991-03-21 1994-12-13 The United States Of America As Represented By The United States Department Of Energy Combined enzyme mediated fermentation of cellulous and xylose to ethanol by Schizosaccharoyces pombe, cellulase, β-glucosidase, and xylose isomerase
US5824246A (en) 1991-03-29 1998-10-20 Engineered Composites Method of forming a thermoactive binder composite
US5173257A (en) * 1991-04-03 1992-12-22 Pearson Erich H Continuous process and apparatus for the separation of recyclable material from and the disinfection of infectious medical waste
US5543205A (en) 1991-06-14 1996-08-06 Corrcycle, Inc. Composite article made from used or surplus corrugated boxes or sheets
US5366790A (en) 1991-06-14 1994-11-22 Liebel Henry L Composite article made from used or surplus corrugated boxes or sheets
US5194461A (en) 1991-06-26 1993-03-16 University Of Northern Iowa Foundation Structural materials from recycled high density polyethylene and herbaceous fibers, and method for production
US5196069A (en) 1991-07-05 1993-03-23 The United States Of America As Represented By The United States National Aeronautics And Space Administration Apparatus and method for cellulose processing using microwave pretreatment
US5374474A (en) 1991-09-26 1994-12-20 Earth Partners, Inc. Composite board and method of manufacture
IT1251723B (en) 1991-10-31 1995-05-23 Himont Inc POLYOLEFINIC COMPOSITES AND PROCEDURE FOR THEIR PREPARATION
US5198074A (en) 1991-11-29 1993-03-30 Companhia Industreas Brasileiras Portela Process to produce a high quality paper product and an ethanol product from bamboo
EP0555509A1 (en) 1992-02-14 1993-08-18 Carl Schenck Ag High-speed tensile testing machine
US5348871A (en) 1992-05-15 1994-09-20 Martin Marietta Energy Systems, Inc. Process for converting cellulosic materials into fuels and chemicals
US5508183A (en) 1992-05-15 1996-04-16 Martin Marietta Energy Systems, Inc. Enhanced attrition bioreactor for enzyme hydrolysis or cellulosic materials
US5372878A (en) 1992-06-23 1994-12-13 Yamasa Momi Kikaku Co., Ltd. Slackened or creased fibrous sheet
US5285973A (en) 1992-07-15 1994-02-15 Advanced Environmental Recycling Technologies, Inc. Close tolerance shredder
US5308896A (en) 1992-08-17 1994-05-03 Weyerhaeuser Company Particle binders for high bulk fibers
US5352480A (en) 1992-08-17 1994-10-04 Weyerhaeuser Company Method for binding particles to fibers using reactivatable binders
US6340411B1 (en) 1992-08-17 2002-01-22 Weyerhaeuser Company Fibrous product containing densifying agent
EP1219744B1 (en) 1992-08-17 2004-10-20 Weyerhaeuser Company Particle binders
CA2100319C (en) 1992-08-31 2003-10-07 Michael J. Deaner Advanced polymer/wood composite structural member
US6004668A (en) 1992-08-31 1999-12-21 Andersen Corporation Advanced polymer wood composite
US5773138A (en) 1992-08-31 1998-06-30 Andersen Corporation Advanced compatible polymer wood fiber composite
US5985429A (en) 1992-08-31 1999-11-16 Andersen Corporation Polymer fiber composite with mechanical properties enhanced by particle size distribution
US5981067A (en) 1992-08-31 1999-11-09 Andersen Corporation Advanced compatible polymer wood fiber composite
CA2100320C (en) 1992-08-31 2011-02-08 Michael J. Deaner Advanced polymer wood composite
US5406768A (en) 1992-09-01 1995-04-18 Andersen Corporation Advanced polymer and wood fiber composite structural component
US5821111A (en) 1994-03-31 1998-10-13 Bioengineering Resources, Inc. Bioconversion of waste biomass to useful products
US5370999A (en) 1992-12-17 1994-12-06 Colorado State University Research Foundation Treatment of fibrous lignocellulosic biomass by high shear forces in a turbulent couette flow to make the biomass more susceptible to hydrolysis
US5298102A (en) 1993-01-08 1994-03-29 Sorbilite Inc. Expanding pressure chamber for bonding skins to flat and shaped articles
US5284610A (en) 1993-02-09 1994-02-08 Kang Na Hsiung Enterprise Co., Ltd. High molecular absorbent sheet manufacturing process and the related equipment
US5441801A (en) 1993-02-12 1995-08-15 Andersen Corporation Advanced polymer/wood composite pellet process
US5350370A (en) 1993-04-30 1994-09-27 Kimberly-Clark Corporation High wicking liquid absorbent composite
FR2704863B1 (en) 1993-05-04 1995-06-23 Simmaco THERMOSETTING COMPOSITION, IN PARTICULAR FOR BODYWORK OF MOTOR VEHICLES, PROCESS FOR OBTAINING SAME AND RECYCLING PROCESS.
US5472651A (en) 1993-05-28 1995-12-05 Repete Corporation Optimizing pellet mill controller
CN1055940C (en) 1993-07-28 2000-08-30 生物技术生物自然包装有限两合公司 Reinforced biodegradable polymer
DE4331747A1 (en) 1993-09-20 1995-03-23 Wuenning Paul Extruded, fiber-reinforced natural material granulate for thermoplastic processing, and process for its production
EP0723698A4 (en) 1993-10-15 1997-11-05 Georgia Power Co Squirrel shield device
US5437766A (en) 1993-10-22 1995-08-01 The Procter & Gamble Company Multi-ply facial tissue paper product comprising biodegradable chemical softening compositions and binder materials
US5516472A (en) 1993-11-12 1996-05-14 Strandex Corporation Extruded synthetic wood composition and method for making same
US5540244A (en) 1993-12-07 1996-07-30 Advanced Environmental Recycling Technologies, Inc. Method and apparatus for cleaning and recycling post-consumer plastic films
US5571703A (en) 1993-12-23 1996-11-05 Controlled Environmental Systems Corporation Municipal solid waste processing facility and commercial ethanol production process
US5791262A (en) 1994-02-14 1998-08-11 The Fabri-Form Co. Reinforced plastic pallet
KR200144868Y1 (en) 1995-01-10 1999-06-15 최진호 Mop fixing device of vacuum cleaner
US5480602A (en) 1994-06-17 1996-01-02 Nagaich; Laxmi Extruded particle board
US5439749A (en) 1994-08-18 1995-08-08 Andersen Corporation Composite wood structure
US5746958A (en) 1995-03-30 1998-05-05 Trex Company, L.L.C. Method of producing a wood-thermoplastic composite material
US5837506A (en) 1995-05-11 1998-11-17 The Trustee Of Dartmouth College Continuous process for making ethanol
US5585155A (en) 1995-06-07 1996-12-17 Andersen Corporation Fiber reinforced thermoplastic structural member
US5932456A (en) 1995-06-07 1999-08-03 Ingram-Howell, L.L.C. Production of ethanol and other fermentation products from biomass
US5677154A (en) 1995-06-07 1997-10-14 Ingram-Howell, L.L.C. Production of ethanol from biomass
US5735916A (en) 1995-07-13 1998-04-07 Lucas; James Lewis Process for production of lignin fuel, ethyl alcohol, cellulose, silica/silicates, and cellulose derivatives from plant biomass
US5876641A (en) 1995-07-31 1999-03-02 Andersen Corporation In-line process for injection of foam material into a composite profile
US5705216A (en) 1995-08-11 1998-01-06 Tyson; George J. Production of hydrophobic fibers
US5643359A (en) 1995-11-15 1997-07-01 Dpd, Inc. Dispersion of plant pulp in concrete and use thereof
US5753474A (en) 1995-12-26 1998-05-19 Environmental Energy, Inc. Continuous two stage, dual path anaerobic fermentation of butanol and other organic solvents using two different strains of bacteria
US5851469A (en) 1995-12-27 1998-12-22 Trex Company, L.L.C. Process for making a wood-thermoplastic composite
US5948524A (en) 1996-01-08 1999-09-07 Andersen Corporation Advanced engineering resin and wood fiber composite
US5819491A (en) 1996-01-22 1998-10-13 L.B. Plastics Limited Modular construction elements
JP3626274B2 (en) 1996-04-09 2005-03-02 アイン・エンジニアリング株式会社 Composite film regeneration processing method and apparatus
EP0956590A1 (en) 1996-04-29 1999-11-17 Parker-Hannifin Corporation Conformal thermal interface material for electronic components
US5882564A (en) 1996-06-24 1999-03-16 Andersen Corporation Resin and wood fiber composite profile extrusion method
US20040005461A1 (en) 1996-07-11 2004-01-08 Nagle Dennis C. Carbonized wood-based materials
US5874263A (en) 1996-07-31 1999-02-23 The Texas A&M University System Method and apparatus for producing organic acids
NZ336455A (en) * 1996-12-20 2001-04-27 Usf Filtration & Separations A method for cleaning porous membranes using a gas bubble system
US5733758A (en) 1997-01-10 1998-03-31 Nguyen; Quang A. Tower reactors for bioconversion of lignocellulosic material
US6357197B1 (en) 1997-02-05 2002-03-19 Andersen Corporation Polymer covered advanced polymer/wood composite structural member
US5948505A (en) 1997-03-28 1999-09-07 Andersen Corporation Thermoplastic resin and fiberglass fabric composite and method
US6333181B1 (en) 1997-04-07 2001-12-25 University Of Florida Research Foundation, Inc. Ethanol production from lignocellulose
US6102690A (en) 1997-04-07 2000-08-15 Univ. Of Florida Research Foundation, Inc. Recombinant organisms capable of fermenting cellobiose
EP1011577A4 (en) 1997-05-13 2004-06-16 Weyerhaeuser Co Reticulated absorbent composite
US6122877A (en) 1997-05-30 2000-09-26 Andersen Corporation Fiber-polymeric composite siding unit and method of manufacture
US5916780A (en) 1997-06-09 1999-06-29 Iogen Corporation Pretreatment process for conversion of cellulose to fuel ethanol
US6130076A (en) 1997-06-19 2000-10-10 University Of Florida Research Foundation, Inc. Ethanol production using a soy hydrolysate-based medium or a yeast autolysate-based medium
US5942424A (en) 1997-06-19 1999-08-24 Lockheed Martin Energy Research Corporation Method for the enzymatic production of hydrogen
US6043392A (en) 1997-06-30 2000-03-28 Texas A&M University System Method for conversion of biomass to chemicals and fuels
US5882905A (en) 1997-08-01 1999-03-16 The United States Of America As Represented By The Secretary Of Agriculture Thermostable α-L-arabinofuranosidase from Aureobasidium pullulans
US5968362A (en) 1997-08-04 1999-10-19 Controlled Enviromental Systems Corporation Method for the separation of acid from sugars
US5952105A (en) 1997-09-02 1999-09-14 Xyleco, Inc. Poly-coated paper composites
US20030187102A1 (en) * 1997-09-02 2003-10-02 Marshall Medoff Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same
US20030032702A1 (en) 1997-09-02 2003-02-13 Marshall Medoff Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same
US5973035A (en) 1997-10-31 1999-10-26 Xyleco, Inc. Cellulosic fiber composites
US20020010229A1 (en) 1997-09-02 2002-01-24 Marshall Medoff Cellulosic and lignocellulosic materials and compositions and composites made therefrom
US6448307B1 (en) 1997-09-02 2002-09-10 Xyleco, Inc. Compositions of texturized fibrous materials
US6054207A (en) 1998-01-21 2000-04-25 Andersen Corporation Foamed thermoplastic polymer and wood fiber profile and member
US6015703A (en) 1998-03-10 2000-01-18 Iogen Corporation Genetic constructs and genetically modified microbes for enhanced production of beta-glucosidase
AU3950799A (en) 1998-04-20 1999-11-08 Forskarpatent I Syd Ab Genetically engineered yeast and mutants thereof for the efficient fermentation of lignocellulose hydrolysates
US6420626B1 (en) 1999-06-08 2002-07-16 Buckeye Technologies Inc. Unitary fluid acquisition, storage, and wicking material
ZA200004369B (en) * 1998-07-02 2002-05-29 Procter & Gamble Carbon fiber filters.
US6270883B1 (en) 1998-10-09 2001-08-07 The United States Of America As Represented By The Secretary Of Agriculture Composites containing cellulosic pulp fibers and methods of making and using the same
US6703227B2 (en) 1999-02-11 2004-03-09 Renessen Llc Method for producing fermentation-based products from high oil corn
US7074603B2 (en) 1999-03-11 2006-07-11 Zeachem, Inc. Process for producing ethanol from corn dry milling
DE60039973D1 (en) 1999-03-11 2008-10-02 Zeachem Inc PROCESS FOR THE MANUFACTURE OF ETHANOL
BR9902606B1 (en) 1999-06-23 2011-04-19 catalytic cellulignin fuel.
US6746976B1 (en) 1999-09-24 2004-06-08 The Procter & Gamble Company Thin until wet structures for acquiring aqueous fluids
US6409841B1 (en) 1999-11-02 2002-06-25 Waste Energy Integrated Systems, Llc. Process for the production of organic products from diverse biomass sources
WO2001032715A1 (en) 1999-11-02 2001-05-10 Waste Energy Integrated Sytems, Llc Process for the production of organic products from lignocellulose containing biomass sources
US6258175B1 (en) 1999-11-03 2001-07-10 Gene E. Lightner Method to produce fermentable sugars from a lignocellulose material
WO2001060752A1 (en) 2000-02-17 2001-08-23 Forskningscenter Risø A method for processing lignocellulosic material
ES2166316B1 (en) 2000-02-24 2003-02-16 Ct Investig Energeticas Ciemat PROCEDURE FOR THE PRODUCTION OF ETHANOL FROM LIGNOCELLULOSIC BIOMASS USING A NEW THERMOTOLERING YEAST.
PT1282686E (en) 2000-05-15 2007-11-07 Scandinavian Technology Group A recombinant yeast for lignocellulose raw materials
US20020019614A1 (en) 2000-05-17 2002-02-14 Woon Paul S. Absorbent articles having improved performance
US20020137154A1 (en) 2000-06-26 2002-09-26 Ingram Lonnie O?Apos;Neal Methods for improving cell growth and alcohol production during fermentation
CA2411479A1 (en) 2000-06-26 2002-01-03 Lonnie O. Ingram Methods and compositions for simultaneous saccharification and fermentation
AU2001265820A1 (en) 2000-07-04 2002-01-14 Neurosearch A/S Steric isomers of fused tropane derivatives and their use as monoamine neurotransmitter re-uptake inhibitors
US20020012980A1 (en) * 2000-07-25 2002-01-31 Wisconsin Alumni Research Foundation Method for simultaneous saccharification and fermentation of spent cellulose sausage casings
US6620503B2 (en) 2000-07-26 2003-09-16 Kimberly-Clark Worldwide, Inc. Synthetic fiber nonwoven web and method
US6423145B1 (en) 2000-08-09 2002-07-23 Midwest Research Institute Dilute acid/metal salt hydrolysis of lignocellulosics
US6596209B2 (en) 2000-08-10 2003-07-22 California Agriboard Llc Production of particle board from agricultural waste
AU2002210409A1 (en) 2000-11-10 2002-05-21 Novozymes A/S Ethanol process
US6908995B2 (en) 2001-01-05 2005-06-21 David H. Blount Production of carbohydrates, alcohol and resins from biomass
JP4077158B2 (en) * 2001-01-10 2008-04-16 株式会社メニコン Plant fiber degrading agent and method for treating plant waste using the same
WO2002057317A1 (en) 2001-01-16 2002-07-25 Biomass Conversions, Llc Disruption of plant material to readily hydrolyzable cellulosic particles
US20030021915A1 (en) 2001-06-15 2003-01-30 Vivek Rohatgi Cellulose - polymer composites and related manufacturing methods
PL197595B1 (en) 2001-07-12 2008-04-30 Kazimierz Chrzanowski Method and system of manufacture of methane and generation of electric and thermal energy
US6835560B2 (en) 2001-10-18 2004-12-28 Clemson University Process for ozonating and converting organic materials into useful products
FI20012091A0 (en) 2001-10-29 2001-10-29 Valtion Teknillinen Fungal microorganism with improved performance in biotechnological processes
US20030125688A1 (en) 2001-11-30 2003-07-03 Keane James M. Adhesive system for mechanically post-treated absorbent structures
US6837956B2 (en) 2001-11-30 2005-01-04 Kimberly-Clark Worldwide, Inc. System for aperturing and coaperturing webs and web assemblies
US6962722B2 (en) 2001-12-04 2005-11-08 Dawley Larry J High protein corn product production and use
US8558058B2 (en) 2001-12-06 2013-10-15 Applied Biotechnology Institute Monocotyledonous seed expressing exo-1,4B-glucanase
AU2002346656A1 (en) 2001-12-06 2003-06-23 Prodigene, Inc. Methods for the cost-effective saccharification of lignocellulosic biomass
US6824682B2 (en) 2001-12-18 2004-11-30 Best Biofuels Llc C/O Smithfield Foods, Inc. System and method for extracting energy from agricultural waste
WO2003062430A1 (en) 2002-01-23 2003-07-31 Royal Nedalco B.V. Fermentation of pentose sugars
JP4001488B2 (en) * 2002-01-28 2007-10-31 アキレス株式会社 Package for carrier chip for immobilizing microorganisms
US6670035B2 (en) 2002-04-05 2003-12-30 Arteva North America S.A.R.L. Binder fiber and nonwoven web
US6743507B2 (en) 2002-06-07 2004-06-01 Rayonier Products And Financial Services Company Cellulose fiber reinforced composites having reduced discoloration and improved dispersion and associated methods of manufacture
US6855182B2 (en) 2002-07-17 2005-02-15 Rayonier Products And Financial Services Company Lignocellulose fiber composite with soil conditioners
GB0218012D0 (en) 2002-08-05 2002-09-11 Ciba Spec Chem Water Treat Ltd Production of a fermentation product
GB0218021D0 (en) 2002-08-05 2002-09-11 Ciba Spec Chem Water Treat Ltd Production of a fermentation product
DK1578964T4 (en) 2002-12-20 2013-12-02 Novozymes As Polypeptides with cellobiohydrolase II activity and polynucleotides encoding the same
CN1788083B (en) 2003-03-10 2011-10-05 诺维信公司 Alcohol product processes
US7604967B2 (en) 2003-03-19 2009-10-20 The Trustees Of Dartmouth College Lignin-blocking treatment of biomass and uses thereof
US20040187863A1 (en) 2003-03-25 2004-09-30 Langhauser Associates Inc. Biomilling and grain fractionation
AU2004236724B2 (en) 2003-05-02 2008-07-10 Cargill Inc. Genetically modified yeast species and fermentation processes using genetically modified yeast
US20040253696A1 (en) 2003-06-10 2004-12-16 Novozymes North America, Inc. Fermentation processes and compositions
CN108486086A (en) 2003-07-02 2018-09-04 维莱尼姆公司 Dextranase, encode they nucleic acid and preparation and use their method
WO2005079190A2 (en) 2003-09-12 2005-09-01 Midwest Research Institute Production of ethanol and high-protein feed co-products from high-solids conversion of cereal grains and legumes
US7504245B2 (en) 2003-10-03 2009-03-17 Fcstone Carbon, Llc Biomass conversion to alcohol using ultrasonic energy
SE526429C2 (en) 2003-10-24 2005-09-13 Swedish Biofuels Ab Intensifying fermentation of carbohydrate substrate for, e.g. producing one to five carbon alcohols, involves using amino acid leucine, isoleucine, and/or valine as source of nitrogen
CA2545981A1 (en) 2003-12-01 2005-06-16 Swetree Technologies Ab Fermentation process, starter culture and growth medium
WO2005069849A2 (en) 2004-01-16 2005-08-04 Novozymes North America, Inc Fermentation processes
WO2005067531A2 (en) 2004-01-16 2005-07-28 Novozymes Inc. Methods for degrading lignocellulosic materials
DK2305703T3 (en) 2004-01-30 2014-06-16 Novozymes Inc Polypeptides with cellulolytic enhancing activity and polynucleotides encoding them
CN1965078B (en) 2004-02-06 2013-09-18 诺维信股份有限公司 Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same
JP4463719B2 (en) * 2004-04-22 2010-05-19 日本特殊陶業株式会社 Organic-inorganic composite porous body, method for producing fibrous organic substance, and method for producing organic-inorganic composite porous body
US20060014260A1 (en) 2004-05-07 2006-01-19 Zhiliang Fan Lower cellulase requirements for biomass cellulose hydrolysis and fermentation
WO2005113459A1 (en) 2004-05-13 2005-12-01 Cornell Research Foundation, Inc. Self-pressurizing, self-purifying system and method for methane production by anaerobic digestion
SE0401303D0 (en) 2004-05-19 2004-05-19 Forskarpatent I Syd Ab Ethanol productivities of microbial strains in fermentation of dilute-acid hydrolyzates depending on their furan reduction capacities
FI118012B (en) 2004-06-04 2007-05-31 Valtion Teknillinen Process for producing ethanol
US6998374B2 (en) 2004-06-14 2006-02-14 Carl Niedbala Composition and method for cleaning gelatin encapsulated products comprising a non-volatile silicone/volatile silicone mixture
ITMI20041646A1 (en) 2004-08-11 2004-11-11 Ocrim Spa PROCEDURE FOR THE PRODUCTION OF ETHANOL WITH THE USE OF CORN FLOURS
WO2006031757A1 (en) 2004-09-10 2006-03-23 Rutgers, The State University Energy production from the treatment of organic waste material comprising immiscible polymer blend membrane
US8309324B2 (en) 2004-11-10 2012-11-13 University Of Rochester Promoters and proteins from Clostridium thermocellum and uses thereof
CA2599577A1 (en) 2005-03-04 2006-09-14 Verenium Corporation Nucleic acids and proteins and methods for making and using them
BRPI0609140A2 (en) 2005-03-15 2010-02-17 Verenium Corp cellulases, nucleic acids that encode them and methods for their production and use
US7708214B2 (en) * 2005-08-24 2010-05-04 Xyleco, Inc. Fibrous materials and composites
EP1869197A2 (en) 2005-04-12 2007-12-26 E.I. Dupont De Nemours And Company Treatment of biomass to obtain ethanol
WO2006113683A2 (en) 2005-04-19 2006-10-26 Archer-Daniels-Midland Company Process for the production of animal feed and ethanol and novel feed
CA2910102A1 (en) 2005-04-26 2006-11-02 Novozymes A/S Hydrolysis of arabinoxylan
US8501463B2 (en) 2005-05-03 2013-08-06 Anaerobe Systems Anaerobic production of hydrogen and other chemical products
AU2006254627A1 (en) 2005-06-03 2006-12-07 Iogen Energy Corporation Method of continuous processing of lignocellulosic feedstocks
US20060292677A1 (en) 2005-06-22 2006-12-28 Brad Ostrander Use of corn with low gelatinization temperature for production of fermentation-based products
US8652817B2 (en) 2005-07-01 2014-02-18 Univeristy Of Florida Research Foundation, Inc. Recombinant host cells and media for ethanol production
CA2959268A1 (en) 2005-07-19 2007-01-25 Inbicon A/S Method and apparatus for conversion of cellulosic material to ethanol
US20090258106A1 (en) * 2005-07-20 2009-10-15 Robert Jansen Corn Wet Milling Process
US20070020375A1 (en) * 2005-07-20 2007-01-25 Robert Jansen Corn wet milling process
US7135308B1 (en) 2006-02-28 2006-11-14 Propulsion Logic, Llc Process for the production of ethanol from algae
US9090915B2 (en) * 2008-04-22 2015-07-28 Wisconsin Alumni Research Foundation Sulfite pretreatment for biorefining biomass
NZ596930A (en) * 2009-05-20 2014-06-27 Xyleco Inc Bioprocessing
US8146841B2 (en) * 2010-07-26 2012-04-03 Glass Processing Solutions, Llc Production of clean glass particles from post-consumer waste

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4237226A (en) 1979-02-23 1980-12-02 Trustees Of Dartmouth College Process for pretreating cellulosic substrates and for producing sugar therefrom
US5705369A (en) 1994-12-27 1998-01-06 Midwest Research Institute Prehydrolysis of lignocellulose
US7901511B2 (en) 2001-02-28 2011-03-08 Iogen Energy Corporation Method of processing lignocellulosic feedstock for enhanced xylose and ethanol production

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2032261A4

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8329455B2 (en) 2011-07-08 2012-12-11 Aikan North America, Inc. Systems and methods for digestion of solid waste
US8492134B2 (en) 2011-07-08 2013-07-23 Aikan North America, Inc. Systems and methods for digestion of solid waste
US9328323B2 (en) 2011-07-08 2016-05-03 Aikan North America, Inc. Systems and methods for digestion of solid waste
US11015059B2 (en) 2019-05-23 2021-05-25 Bolt Threads, Inc. Composite material, and methods for production thereof
US11891514B2 (en) 2019-05-23 2024-02-06 Bolt Threads, Inc. Composite material, and methods for production thereof

Also Published As

Publication number Publication date
NZ609636A (en) 2014-07-25
AU2007257741B2 (en) 2010-07-15
US20130334725A1 (en) 2013-12-19
EP3135379B1 (en) 2019-02-27
EP2032261A2 (en) 2009-03-11
CN101541432A (en) 2009-09-23
MX342620B (en) 2016-10-06
HUE028695T2 (en) 2016-12-28
US20130189738A1 (en) 2013-07-25
MY159431A (en) 2017-01-13
SI2032261T1 (en) 2016-05-31
RU2434945C2 (en) 2011-11-27
HUE038356T2 (en) 2018-10-29
PL3012025T3 (en) 2018-07-31
PL2032261T3 (en) 2016-07-29
US8544773B2 (en) 2013-10-01
EP3492173A2 (en) 2019-06-05
CA2655111A1 (en) 2007-12-21
BR122017001646B1 (en) 2019-10-22
AU2007257741A1 (en) 2007-12-21
KR20090023684A (en) 2009-03-05
EP2032261A4 (en) 2013-04-10
BRPI0713417A2 (en) 2012-03-27
DK3012025T3 (en) 2018-06-14
BRPI0713417B1 (en) 2019-04-02
EP3012025B1 (en) 2018-04-25
MY147493A (en) 2012-12-14
AP2464A (en) 2012-09-14
EA013498B1 (en) 2010-04-30
ES2558308T3 (en) 2016-02-03
US20110244533A1 (en) 2011-10-06
CN103131483A (en) 2013-06-05
US8413915B2 (en) 2013-04-09
US7708214B2 (en) 2010-05-04
IL195910A (en) 2013-10-31
EP3012025A3 (en) 2016-08-03
NZ598177A (en) 2013-08-30
AP2008004725A0 (en) 2008-12-31
US7980495B2 (en) 2011-07-19
EA200970015A1 (en) 2009-06-30
RU2009101224A (en) 2010-07-20
US20180339428A1 (en) 2018-11-29
LT3012025T (en) 2018-06-11
DK2032261T3 (en) 2016-03-14
IL228131A (en) 2015-07-30
UA93719C2 (en) 2011-03-10
IL228130A (en) 2015-05-31
EP2032261B1 (en) 2015-12-30
MX2008016029A (en) 2009-02-20
WO2007146922A3 (en) 2009-02-26
EP3135379A1 (en) 2017-03-01
ZA200900054B (en) 2009-12-30
US20100267097A1 (en) 2010-10-21
NZ620525A (en) 2015-08-28
US20070045456A1 (en) 2007-03-01
PL3135379T3 (en) 2019-08-30
ES2674252T3 (en) 2018-06-28
IL195910A0 (en) 2009-09-01
EP3492173A3 (en) 2019-09-11
KR101159628B1 (en) 2012-06-27
TR201807349T4 (en) 2018-06-21
CA2655111C (en) 2013-01-08
SI3012025T1 (en) 2018-06-29
MY159433A (en) 2017-01-13
BR122018075069B1 (en) 2019-07-16
US8757525B2 (en) 2014-06-24
EP3012025A2 (en) 2016-04-27

Similar Documents

Publication Publication Date Title
US20180339428A1 (en) Fibrous materials and compositions
EP1877192B9 (en) Method of making fibrous material
US10059035B2 (en) Fibrous materials and composites
AU2018200906A1 (en) Fibrous materials and composites
AU2013203464B2 (en) Fibrous materials and composites

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 200780028905.8

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 07798424

Country of ref document: EP

Kind code of ref document: A2

ENP Entry into the national phase

Ref document number: 2655111

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 195910

Country of ref document: IL

WWE Wipo information: entry into national phase

Ref document number: 2008121997

Country of ref document: EG

WWE Wipo information: entry into national phase

Ref document number: MX/A/2008/016029

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 573705

Country of ref document: NZ

WWE Wipo information: entry into national phase

Ref document number: 2007257741

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: 1020097000485

Country of ref document: KR

WWE Wipo information: entry into national phase

Ref document number: 2007798424

Country of ref document: EP

Ref document number: 200970015

Country of ref document: EA

ENP Entry into the national phase

Ref document number: 2009101224

Country of ref document: RU

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 255/CHENP/2009

Country of ref document: IN

ENP Entry into the national phase

Ref document number: 2007257741

Country of ref document: AU

Date of ref document: 20070612

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: PI0713417

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20081215