Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS2947655 A
Publication typeGrant
Publication dateAug 2, 1960
Filing dateApr 21, 1955
Priority dateApr 21, 1955
Publication numberUS 2947655 A, US 2947655A, US-A-2947655, US2947655 A, US2947655A
InventorsLee E Eberhardt
Original AssigneeBauer Bros Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of producing wood pulp
US 2947655 A
Images(1)
Previous page
Next page
Description  (OCR text may contain errors)

Aug. 2, 1960 l.. E. EBERHARDT 2,947,655

METHOD oF PRoDucING woon PULP Filed April 21, 195s PULP wooo, Naan Wurz, En. PULP wooo, wenn Hns'r, Erc.

Y omnes f l cmrrzn "l Y 0H 0n amsn GHzmcnLs 'En-Marla #grama IF Necrssnny yy wirr/Nq on saam? an SIMILE Rarnny Pnzss "2. wnren 3 Exruncreso Algun-#MLS r mucr L h R01-any Fuss ,1 3y HTTnlr/onl MlLl. 4

WATER y hr1-mno MILL 4- HrrmrloN MILL 15' A gun-rs T. F5

llrrlrlo/v MILL 6' su," csnrnlruqnL cunas* R F y Ears 1b Rsascrs n 5535- CmrRlrUqnLCLen/ RUIM/,q Rav/my ScReN` 7 Cinouun wooo PULP 69. -2

HrTRlTlo/v MILI."4

GRQUND woon PULP v af/gf] RrrnlTloN MILL 1'4 Rar/my ScnEEN,

Hrrmmm MILL '6' 1 Rulers Fon l rTmT/o/v MILL "5 kzfmmg ,qvrmrlou MILL 1 Nor/Ry ScREEN ,-7 sL'wL-R deurmrUqnL CL :nnen 6 r 6 0 To an F Mfeumruqn cumul! mamma CLEANER 6 Fm/ms r 7 Rgrgky SCREEN Qrowvo woao PULP Gnou/vn wooo PULP g/rg Cikouna waan PULP L 4 INVENTOR.

Les E. Enna/MDT 2,947,655 METHOD F PRODUCING WGOD PULP Lee E. Eberhardt, Springield, Ohio, assignor to The Bauer Bros. Company, Springfield, Ohio, a corporation of hio Filed Apr. 21, 1955, Ser. No. 502,980

13 Claims. (Cl. 162-26) This invention relates to the production of wood pulp and more particularly to the apparatus and method for producing a wood pulp comparable to groundwood.

Groundwood pulp is now produced by grinding or abrading barked logs. In practice the wood is generally cut in four foot lengths, the bark removed therefrom and sorted as to straight and crooked wood. Crooked wood, for example, branches, deformed limbs, and the like, is not suitable for the production of groundwood bythe normal process since it cannot be eiectively or satisfactorily held in contact engagement with the face of the abrading or grinding wheel. The grinder is generally a relatively large machine having an abrasive stone with a four foot wide peripheral face, against which the logs are placed with their taxes parallel to the axis of the stone. The logs, when held under pressure in contact with the moving face of the stone, are abraded to thereby produce a collection of fibers.

It has been found that a pulp comparable in quality to groundwood can be produced by making chips of the raw wood, passing these chips through a rotary press in which pressure is successively applied and removed during travel of the chips through the press, and then completing the iiberizing of the chips material in a disc mill or rener. The quality of the pulp so produced is equal to, or in some instances better than, that produced by the conventional method and such pulp is produced at a considerablesavings in power requirements.V

A further advantage of the process is that it permits the use of small diameter wood, crooked wood, slabs, edgings, and other forms of wood which are either impossible or impractical to use inthe conventional processing of groundwood. t

The present invention involves not only a new process for the manufacture of pulp comparable to groundwood but the discovery of the adaptability and usefulness Vof conventional equipment for the production of a groundvvood type pulp. The equipment used in the present process for the production of groundwood type pulp is entirely rdifferent than any that has heretofore been used for this purpose. It is nevertheless `standard equipment in Ithat it -is well known for other applications. When used in accordance with the present process an entirely new and unexpected result is obtained. Considerable advantage `is gained over the conventional methods and apparatus for producing groundwood pulp.` Such advantage is three-fold, namely, first, use of conventional equipment eliminates the necessity for speciality equipment such as the grinding wheel and its associated equipment, second, considerable less -power is required, and third, scrap wood and other types of wood heretofore unusable for production of 4groundwood are now made usable. p

Thus, the object of the invention is to improve the con struction as well as the means and method of operation offgroundwood pulp mills as disclosed herein, whereby such groundwood pulp may not only be more economically manufactured but will provide more eificient utilization of power and wood supply.

A further object of the invention is to provide means whereby multipurpose equipment can be used for the manufacture of groundwood pulp.

A further object of the invention is to provide a new process by means of which groundwood pulp can be made with conventional equipment.

A further object of the invention is to provide a means and a process for producing groundwood pulp which will provide more efficient utilization of the raw wood material from which the groundwood pulp i-s made.

A further object of the invention is to provide a means and a process for producing groundwood pulp with less power consumption than is now normal.

A further object of the invention is to provide a means and a process whereby a complete utilization of the raw material may be achieved.

A further object of the invention is to provide a means and process for producing groundwood pulp wherein waste or lost material is relatively small.

A further object of the invention is to provide a means and process for the production of groundwood pulp which will produce desirable by-products in a form which can be utilized.

A further object of the invention is to provide a means and process for producing groundwood type pulp posssing the advantageous features, the inherent meritorious characteristics and the mode of operation herein described.

With the above primary and other incidental objects in view as will more fully appear in this speciiication, the invention intended to be protected by Letters Patent consists of the features, the parts and combinations thereof, and the mode of operation and process as hereinafter described or illustrated in the accompanying drawing, or their equivalents.

Referring to the accompanying drawing wherein is shown ilow diagrams of the preferred but obviously not necessarily the only forms of embodimentV of the invention:

Fig. 1 is a diagrammatic ilow chart of one form of the invention;

Fig. 2 is a flow chart similar to Fig. 1, but having one step in the process eliminated;

Fig. 3 is a portion of the chart shown in' Figs. 1 and 2 with a reversal in sequence of two of the steps;

Fig. 4 is 4a portion of the ow chart of Figs. 1 and 2 showing an optional return of rejects, which may be incorporated in the charts of Figs. l and 2 or the modication of Fig. 3; and

Fig. 5 is a diagrammatic flow chart of a further modication of the process shown in Fig. l.

Like parts are indicated by similar characters of reference throughout the several views.

Referring to the drawings there is shown in Fig. 1 a ow diagram for the typical installation incorporating the present process for the production of groundwood type pulp. The raw wood, wood waste, edgings, slabs and the like are fed to a chipper 1 wherein the raw wood of whatever type, is chipped or' broken into relatively small pieces. Such cln'p'pers,- although possibly varying to some extent in detail construction, all operate on the same principle. The raw wood is advanced to a cutting mechanism which in effect slices from the end of the log, slab, or the like a thin slice. This slice as it falls by gravity breaks into small 'chips or pieces. These chipsor pieces are then collected for further processing.

The chips are taken from the chipper and placed in a soaking vat where moisture is reintroduced Vinto the chips and all chips are brought to a common level of moisture content. Depending upon the typeof chips 3 being processed, the inclusion in this soaking vat of a wetting agent or a weak chemical solution such as a weak solution of sodium hydroxide or other softening agents. may bedesirable.

This soaking or wetting step is not necessary in all instances.. It is, however, desirable when the wood being processed is veneer or kiln dried lumber waste which wood is extremely dry. The iiow diagram for the process without the inclusion of the wettingstep isshown in Fig. 2.

The chips are then taken `from the wetting vat at a uniform level of moisture,` and placed in a rotary press .'1.V In the event the soaking step Vis omitted (Fig. 2) thechips-as they come from the chipper are at a substantially uniform moisture level and can-be fully'- and properly processed in the press 3 the same as if they had undergone the wetting step. The rotary press 3 is of a screw type similar to that which has been heretofore used in the oil industry for extraction of oil from cotton seed,- tungnutsl and the like. The particular press used herein involves a succession of pressure applications and releases during travel of the wood material through the press. The material being processed is compressed by the rotation of a helical'feed screw and gradually advanced through a restricted area. As the material passes the restricted area itis permitted to expand where pressure is released.l As pressure is released the feed screw again picks up the material and again presses or applies pressure thereto in the advancement of the material past a further restricted area. During thepressing of the wood it is subjected not only to pressure but also to a twisting or shearing action due to the rotary motion of the feed screw. The material within the press is therefor subjected simultaneously to a squeezing and shearing action and to the successive application and release of relatively high pressures. Such treatment ofthe material extracts Vtherefrom the greater part of the moisture and in addition thereto some ofthe natural wood uids such as'sap, rosin, and chemicals normally present in the wood. The lignin and other wood sugars areV also softened during this pressing operation.

During such extraction of these materials a certain degreefofheat is developed in the press which materially assists in the processing of the wood and the satisfactory extraction of these other compounds. The heat developed, however, is not comparable to that of the normal cooking operation as is generally used in theprocessing'of bers for pulp purposes.

The material extracted from the wood chips during the pressing operation' may be later separatedor classied and subsequently disposed of as by-products of the present process.

The rotary press causes a breakdown-of the chipped material and an opening up of the iiberous structure thereof.. A high degree of iberizing, maceration or brillation is achieved by the successive application and release of pressure combined with the squeezing and shearing produced by the rotary screw member. The material, as it is discharged from the press, is in excellent condition for further refining or treatment to produce a ground wood type of pulp by conventional attrition means.

AsV the partially berized chips are discharged from lrotary'press the fibers thereof are immediately rewet or moistened either with water or .a vapor so as to prevent damage thereto during handling. It is preferable that some wetting or moistening of the material take place at the point of inal pressure release in therotary press since at: this point the material is eXtreme receptive to the introduction of the moisture and will readily absorp it.

The moistened material is then transferred to a conventional attrition mill. During such transfer, additional waterV is added thereto so as to produce a mixture suitablefor further refining in the attrition mill.

The attrition mill 4 is preferably of the disc type and maybeof any conventional design, `i.e. a singleI disc lmillV or a double disc mill. The partially tiberized material is subjected to a high degree of fiberizing action in the attrition mill which produces a long ibrous material generally similar in overall quality to that normally used in insulation board material. However, mixed in with the long hers are numerous short length fibers and also probably some long shives. Shi'ves are groups of fibers which have not beenfully Aseparated-by theY processing to this point.

The material as it comes-from -attrition mill-.4 is then The output of the second `stage renner 5 'is of the type commonly used in newsprint, lower quality book papers and the like, and constitutes a pulp which is in quality equal to or better than the Yuormallyprduced ground wood pulp.

The pulp as. it is discharged from'thesecondretining.

stage -is introduced into a centrifugal cleanerl 6. The cleaner 6V effects a substantiallycornplete removal of dirt, bark specks, short stubby iibers or shor-t and stubbyshives. Also removed by the centrifugal cleaner are all inorganic or Vforeign organic materialsv which would reduce .thepulp quality. The material rejected by-the centrifugal cleaner 6 is discharged to waste, as--shown in Fig-1, while the material accepted or passed by the centrifugal cleaner is conveyed toarotary` screen 7.

The rotary screen grades the pulp,- ,separatingtherefrom-v as rejects any long shives, clusters ofunseparated fibersv and the like.- Such material as is rejected by the rotary screen 7 is returned to the rotary press 3 (Fig-l) for furtherrening where itis Amixed in withrthe-new chips being introduced to the press and proceedsithrough the same process as has heretofore been described; The material passed by the rotary screenas acceptable is collected and comprises the nished pulpof the groundwood type.

The finished pulp, while beingof the groundwood type and equal thereto in quality, has nevetheless been produced from waste woodor wood of inferior grades,` and has been produced with the expenditure' of considerably less power than is normally required. Furthermore,.it

has been produced through the use of conventional equipment which may be Vused and in fact'is-concurrently-being used for Ypurposes otherthan the-production of groundwood type pulp.

Referring to Fig. 2 of 'the-drawing, this'ow diagramshows substantially the same process as has'heretoforebeen described exceptforthe omissionof 'the'wetting or soaking vat 2. The process shown in Fig. 2 can be advantageously utilized vin instances where the wood as it comes from the chipper has a reasonably high and uni-Y process of Fig. l involving areve'rsal of the last twoV steps in said process as shownj in Fig. 1; In Fig. 3 the rotary screen 7 receives-the discharge from thes'econd stage rener 5 and grades thepulp byfseparation therefrom ofthe-long-'shives and' clustersV of unseparated-fibers priortothe cleaning of thepulp. The'- material acceptedbyA the screen 7- is then introduced-into-the cleaner 6- for the removal of dirt, bark specks and the like. The-material rejected by the screen 7 isreintroduced into the process forrefiningwhile the-material rejected by the cleaner 6 isdirected-to the seweras--waste material.A This' modificationofthe process off-Fig. 1 -is advantageousz when using woods which are relatively hard to fibrillate or separate into individual fibers. By use of the process of Fig. 3, the long shives and undefibered material are removed prior to the cleaning of the pulp. This permits use of less cleaning capacity inasmuch as the entire volume is not passing through the cleaner.

Depending upon the Vamount of re-refining required to separate the long shives and clusters of undefibered material rejected by the screen 7, such rejects may be reintroduced into the rotary press 3, as shown in Fig. l, or reintroduced into the first refining stage or mill 4, as shown in Fig. 4. Where the amount of re-refining needed is not extensive, the modification of Fig.v 4 has been found quite successful. In this form of the process the rejects from the screen 7 are introduced into mill 4 along with the material discharged from the rotary press 3 and they then proceed through the process again. The reversal of the cleaner 6 and screen 7, as shown in Fig. 3, may also be made in the modification of Fig. 4. Such change in Fig. 4 would be made for the same reasons and would produce the same results as previously explained in connection with Fig. 3.

Fig. 5 shows a further modification of the basic process of Fig. 1 which may be advantageously used in certain circumstances determined primarily by the type of wood being used. In this modification, the screen or grading member 7 is interposed between the first stage refining mill 4 and the second stage refining mill 5. As previously noted, the `material as it leaves the first stage mill 4 contains a certain quantity of short fibers. If it is desirable to take precautionary measures to prevent over-refining of the acceptable portion, the stock may be led directly to the centrifugal cleaner 6. In so doing the second stage refiningA mill 5 is completely by-passed by the acceptable portion of the stock discharged from refining mill4. To accomplish this the grading screen 7 is interposed between the mills 4 and 5 with the long shives and clusters of unseparated fibers forming the rejects from the screen 7 being introduced into the second refining mill 5 for further refining action. The acceptable portion from the screen 7 lay-passes the second mill 5 and is introduced into the cleaner 6 simultaneously with the introduction of the material thereto from the second refining mill 5. Thus, any danger of over-refining of the pulp material is obviated.

'I'he modification of Fig. 5 is well suited for use when treating woods which are easily separated or fibrillated.

In view of the foregoing it will be appreciated that there has been evolved a completely new process for the production of groundwood type pulps utilizing machines which although conventional in design and well known for other purposes have never before been known or used for the production of groundwood type pulp. Thus, not only does the present invention include a new process for the production of groundwood type pulp but further includes a new result obtained through the use of old machines and a new product created thereby.

From the above description it will be apparent that there is thus provided a device of the character described possessing the particular features of advantage before enumerated as desirable, but which obviously is susceptible of modification in its form, proportions, detail construction and arrangement of parts without departing from the principle involved4 or sacrificing any of its advantages.

While in order to comply with the statute the invention has been described in language more or less specic 4as to structural features, it is to be understood that the invention is not limited to the specific features shown, but that the means and construction herein disclosed comprise but one of several modes of putting the invention into effect, and the invention is therefore claimed in any of its forms or modifications Within the legitimate and valid scope of the appended claims.

Having thus described my invention, l claim:-

l. The method of producing groundwood pulp consisting of the steps of chipping pulp wood, waste wood and the like, wetting and soaking said chips, subjecting said soaked chips to alternate continuous application and release of mechanically applied pressure for a predetermined period to effect a high degree of fiberization of said chips and extract substantially all the moisture and natural wood uids therefrom in a single pass, introducing water to said chips ,upon final release of pressure, subjecting said pressed chips with water added thereto to a further fiberizing action in a disc mill, discharging said fiberized chips into a centrifugal cleaner for the removal of impurities, dirt specks and the like, the rejects from said cleaner being discharged to waste, subjecting the accepted portion of said stock to the action of a rotary screen for removal of long shives and undefibered chips, the stock removed therefrom being :returned to the pressure stage of the process for further processing, the finally accepted material being acceptable groundwood pulp.

2. The method as set forth in claim 1, characterized by the addition of sodium hydroxide or its equivalent for the softening of lignin, sugars and other compositions in the chips simultaneously with the wetting or soaking of the chips.

3. The method of producing groundwood pulp comprising the steps of chipping pulp wood, waste wood and the like, wetting and soaking said chips, subjecting said soaked chips to continuous alternate application and release of mechanically applied pressure-for a predetermined period to effect a 'high degree of fiberization of said chips and extract substantially all the moisture and natural wood fluids therefrom in a single pass, introducing water to said chips upon nal release of pressure, subjecting said pressed chips with water added thereto to a fiberizing action in a disc mill, cleaning and separating said fiberized chips by use of a centrifugal cleaner and a rotary screen, the material retained after such cleaning being acceptable groundwood pulp, the rejected material from said centrifugal cleaner being waste and the rejected material from said rotary screen being reintroduced in the processing at the disc mill or prior thereto.

4. The method set forth in claim 3, characterized by a reversal of the centrifugal cleaning and rotary screening steps, whereby the material as it comes from the disc mill is subjected rst to the rotary screen and then to the centrifugal cleaner.

5. A process for producing groundwood pulp from raw uncooked Wood, wood waste or the like, consisting of chipping the raw wood, introducing said chips into a rotary mechanical press, subjecting said chips to a series of pressure applications, there being a complete release of pressure intermediate successive pressure applications, said treatment being effected during rotary movement of the chips through the press thereby causing a break down of chip structure and an opening up of the fibrous structure of the chips, the natural wood iiuids and chemicals being extracted from the chips during passage through the press, immediately moistening the fiberized chips as they are discharged from the press, adding additional water thereto and subjecting the moistened tiberized chips with the additional water to a staged disc mill refining operation, and cleaning and grading the fibers after refining.

6. The process set forth in claim 5, characterized by a rotary screening of the refined berized chips intermediate the stages of the refining operation, material rejected in the process being further refined and the accepted material being directly introduced to Acleaning equipment.

7. The process set forth in claim 5, characterized by the rejects from the grading operation being returned to the beginning of the processing in the refining operation.

8. The process set forth in claim 5, characterized by the rejects from the grading operation being re-introduced into the mechanical press.

9. A continuous flow system for the making of groundwood pulp vconsisting 'ofa wood chipper, means operatively connected rthereto Yfor .wetting the chips made'by saidchipper, arotary screw type press operatively connected to-said chipper in following relation thereto wherein the chips aresubjected to successive pressure increases and decreases during rotary and longitudinal travel of the chips through the .pressrto produce a fibrous. material substantially free of liquid, means connected for adding water to the fibrous material as it is discharged from the press, refining means operatively connected to the press for acting upon said fibrous material in successive stages, a vcleaner operatively connected to said refining means to which the refined fibrous material is discharged, and a grader connected for receiving the acceptable material from the cleaner.

l0. A continuous iiow system for the making of groundwood pulp consisting of a wood chipper, means for wetting the chips made by said chipper connected therewith, a rotary screw type press connected to receive the wetted chips and subject them to successive pressure increases and decreases during concurrent rotary and longitudinal travel of the chips through the press to produce a fibrous material, means connected for adding water to the fibrous material as it is discharged from the press, refining means `operatively connected to the press for acting upon said fibrous material in successive stages, means connected for cleaning and grading the fibrous material discharged from the refining means, and means connected with the last named means for re-introducing a portion of the graded fibrous material to the refining means. Y

1l. A continuous flow process for producing groundwood pulp from'raw uncooked wood consisting of the steps of chipping the raw wood, wetting the chips under conditions of substantially atmospheric pressure and temperature, fiberizing the chips in a rotary screw type press by successive applications and release of pressure during continuous `concurrent rotary and longitudinal traveltherethrough, refining-the fiberized materialgand finally grading and cleaning the refined berized material. '12. The process set forth in claim y11, characterized bythe addition of water to the fiberized material prior to the refining thereof, and the refiberation ofithe vmaterial rejected by the grading operation. n M

13. A method of producing groundwood pulp of..waste wood consisting ofthe steps of chipping the wood, Wetting and soaking said chips, subjecting said .chips `to a simultaneous rotary and longitudinal flow while effecting a squeezing Aand shearing thereof in V'successive lintermittentffashion to extract the moisture Tand vother liquids ytherefrom and add a degree of ,heat theretosthereby, introducing waterY to the` partially fiberized chipsresultrefining the Vchips with Water added theretoxin :an attrition -mill to further fiberizesaid chipsto'na Adegree suitable for insulation V:board material, subjecting .said fiberized material 'to a second stage rener berizingvaction to produce pulp usable in newsprint, and subjecting the/product of the second stage refner to aV centrifugal cleaning and rotary screening action to'provide a. finished pulp having a high and uniform quality, Ythe/rejects being returned for further refining.

References-Cited in the tile of this patent UNITED STATES PATENTS Aronovsky et val Y'May 10, 1955

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US223670 *Sep 27, 1879Jan 20, 1880 Manufacture of paper-pulp from wood
US1505934 *Dec 15, 1921Aug 19, 1924Olier Sa Ets ADevice for the continuous treatment of ligneous materials for their transformation in cellulose
US1843467 *Dec 29, 1928Feb 2, 1932Mead Res Engineering CompanyPaper manufacture
US1850832 *Jun 13, 1925Mar 22, 1932Insulite CoProcess of separating wood fibers
US1865768 *Nov 30, 1929Jul 5, 1932Per KlemMethod of treating mechanical wood pulp
US1936697 *Jul 11, 1931Nov 28, 1933Mead Res Engineering CompanyPaper manufacture
US2029973 *Aug 22, 1934Feb 4, 1936Gerald D MuggietonPaper pulp making process
US2030653 *Dec 18, 1931Feb 11, 1936Int Paper CoFireproofing
US2425024 *Nov 21, 1942Aug 5, 1947Paper And Ind Appliances IncApparatus for producing pulp from cellulosic material
US2708160 *Aug 17, 1949May 10, 1955Aronovsky Samuel IProcess for pulping
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3016324 *Mar 7, 1957Jan 9, 1962Bauer Brothers CompanyMethod and apparatus for producing wood pulp
US3073737 *Oct 8, 1958Jan 15, 1963Dorr Oliver IncWood pulp and process for producing same
US3186899 *Sep 11, 1962Jun 1, 1965Minnesota And Outario Paper CoGroundwood pulp
US3224925 *May 21, 1962Dec 21, 1965Cons Paper Bahamas LtdFibrous products from barking waste
US3254847 *Jun 29, 1965Jun 7, 1966Cons Paper Bahamas LtdMethod for treatment of barking waste
US3311308 *Jul 14, 1964Mar 28, 1967Ct Tech De L Ind Des PapiersProcess and apparatus for the refining of fibers used in the manufacture of paper
US3372879 *Aug 18, 1966Mar 12, 1968Cons Paper Bahamas LtdProcess for making a mechanical pulp from wood chips
US3718285 *Dec 3, 1970Feb 27, 1973Bang EProduction of long chips and products made from same
US3989588 *Feb 10, 1975Nov 2, 1976The Bauer Bros. Co.Apparatus for producing kraft type pulp
US4002528 *Dec 15, 1975Jan 11, 1977Kamyr, Inc.Apparatus for processing pulp
US4231526 *Dec 29, 1978Nov 4, 1980J. M. Voith GmbhRough pulping, separation, vibration sorting
US4388148 *Jun 23, 1981Jun 14, 1983Nalco Chemical CompanyProcess for producing pulp
US5405499 *Jun 24, 1993Apr 11, 1995The Procter & Gamble CompanyCellulose pulps having improved softness potential
US5582685 *Aug 9, 1994Dec 10, 1996The Procter & Gamble CompanyMethod for producing a cellulose pulp of selected fiber length and coarseness by a two-stage fractionation
US5679218 *Mar 13, 1996Oct 21, 1997The Procter & Gamble CompanyTissue paper containing chemically softened coarse cellulose fibers
US6817556 *Apr 24, 2002Nov 16, 2004Rolf HeschMethod and apparatus for separating used materials from one another and into reusable components particularly for recycling wood products, used furniture, automobile composite material and similar products
US7726592Dec 2, 2004Jun 1, 2010Hercules IncorporatedProcess for increasing the refiner production rate and/or decreasing the specific energy of pulping wood
USRE31862 *Mar 22, 1983Apr 9, 1985Sunds Defibrator, Inc.Apparatus for the treatment of lignocellulosic material
Classifications
U.S. Classification162/26, 241/42, 241/24.2, 241/28, 241/80, 162/236, 162/28
International ClassificationD21B1/36, D21B1/12
Cooperative ClassificationD21B1/12, D21B1/36
European ClassificationD21B1/12, D21B1/36