CA2520163A1 - An apparatus for producing alkyl ester - Google Patents

An apparatus for producing alkyl ester Download PDF

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Publication number
CA2520163A1
CA2520163A1 CA002520163A CA2520163A CA2520163A1 CA 2520163 A1 CA2520163 A1 CA 2520163A1 CA 002520163 A CA002520163 A CA 002520163A CA 2520163 A CA2520163 A CA 2520163A CA 2520163 A1 CA2520163 A1 CA 2520163A1
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Canada
Prior art keywords
alkyl ester
reactant
reaction product
reaction
inlet
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Granted
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CA002520163A
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French (fr)
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CA2520163C (en
Inventor
Chih-Chung Chou
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Sunho Biodiesel Corp
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Sunho Biodiesel Corp
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Publication of CA2520163A1 publication Critical patent/CA2520163A1/en
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Expired - Fee Related legal-status Critical Current
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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/03Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
    • 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
    • C12P7/62Carboxylic acid esters
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/003Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/04Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
    • C11C3/10Ester interchange
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling of unreacted starting or intermediate materials
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T50/00Aeronautics or air transport
    • Y02T50/60Efficient propulsion technologies, e.g. for aircraft
    • Y02T50/678Aviation using fuels of non-fossil origin

Abstract

An apparatus that includes a first reactor and a return mechanism. The first reactor has an inlet to receive a mixture comprising a first reactant, a second reactant, a reaction product, and an inert solvent that dissolves at least a portion of the first and second reactants, an enzyme to facilitate a reaction between the first and second reactants to generate more reaction product, and an outlet to output the reaction product, including the reaction product received at the inlet and the reaction product generated from the reaction between the first and second reactants. The return mechanism sends at least a portion of the reaction product from the outlet back to the inlet.

Claims (50)

1. An apparatus comprising:
a first reactor having an inlet to receive a mixture comprising a first reactant, a second reactant, a reaction product, and an inert solvent that dissolves at least a portion of the first and second reactants, an enzyme to facilitate a reaction between the first and second reactants to generate more reaction product, and an outlet to output the reaction product, including the reaction product received at the inlet and the reaction product generated from the reaction between the first and second reactants; and a return mechanism to send at least a portion of the reaction product from the outlet back to the inlet.
2. The apparatus of claim 1 in which the reaction product comprises alkyl ester.
3. The apparatus of claim 2 in which the return mechanism sends at least a portion of the alkyl ester back to the inlet.
4. The apparatus of claim 2 in which the mixture includes a solvent that dissolves at least a portion of the first reactant, the second reactant, and the reaction product.
5. The apparatus of claim 4 in which the outlet outputs at least the alkyl ester, the solvent, and unreacted first reactant.
6. The apparatus of claim 5, further comprising an evaporator to evaporate the solvent to generate a mixture comprising the alkyl ester and the unreacted first reactant.
7. The apparatus of claim 5 in which the outlet also outputs glycerol.
8. The apparatus of claim 7, further comprising an evaporator to evaporate the solvent to generate a mixture comprising the alkyl ester, the glycerol, and the unreacted first reactant.
9. The apparatus of claim 8, further comprising a phase separator to separate the alkyl ester from the glycerol based on liquid-liquid phase separation.
10. The apparatus of claim 1 in which the first reactant comprises triglyceride.
11. The apparatus of claim 1 in which the first reactant comprises a carboxylic acid.
12. The apparatus of claim 1 in which the second reactant comprises at least one of a primary and secondary alcohol.
13. The apparatus of claim 1 in which the first reactant comprises at least one of vegetable oil and animal fat.
14. The apparatus of claim 13 in which the reaction product has a composition that is suitable for use as fuel.
15. The apparatus of claim 1, further comprising a second reactor having an inlet to receive a mixture comprising additional second reactant and reaction product from the outlet of the first reactor from the outlet of the first reactor, an enzyme to facilitate a reaction between the second reactant and the other components to generate more reaction product, and an outlet to output the reaction product, including the reaction product received at the inlet of the second reactor and the reaction product generated from the reaction between the second reactant and the other components.
16. The apparatus of claim 15, further comprising an evaporator to evaporate the inert solvent and at least one of unreacted first reactant and unreacted second reactant.
17. The apparatus of claim 16, further comprising a short-path evaporator to separate the reaction product from remaining unreacted reactant.
18. The apparatus of claim 17 in which the reaction product comprises alkyl ester.
19. The apparatus of claim 18, further comprising a return mechanism to send at least a portion of the alkyl ester from the outlet of the second reactor back to the inlet of the first reactor.
20. An apparatus comprising:
a reactor having an inlet to receive a mixture comprising reactants, an enzyme to facilitate a reaction between the reactants, and a feedback mechanism to send at least a portion of a product of the reaction back to the inlet.
21. The apparatus of claim 20 in which the product of the reaction comprises alkyl ester, and the feedback mechanism sends at least a portion of the alkyl ester back to the inlet.
22. The apparatus of claim 20, in which the reactants comprise (1) at least one of triglyceride and carboxylic acid, and (2) at least one of primary and secondary alcohol.
23. The apparatus of claim 20 in which the enzyme comprises a lipase.
24. A system for generating alkyl ester comprising:
a first subsystem including a first reactor having a first inlet to receive a first mixture comprising a first reactant, a second reactant, and an inert solvent to dissolve the first and second reactants, a first enzyme to facilitate a reaction between the first and second reactants to generate a reaction product, and a first outlet to output the reaction product, the inert solvent, and other components; and a second subsystem including a second reactor having a second inlet to receive a second mixture comprising additional second reactant, an inert solvent, at least a portion of the reaction product, and the other components from the first outlet, a second enzyme to facilitate a reaction between the second reactant and the other components to generate more reaction product, and a second outlet to output the reaction product, including the reaction product received at the inlet of the second inlet and the reaction product generated from the reaction between second reactant and the other components.
25. The system of claim 24 in which the reaction product comprises alkyl ester.
26. The system of claim 25 also comprising a return mechanism to send at least a portion of the alkyl ester from the first outlet back to the first inlet.
27. The system of claim 25 also comprising a return mechanism to send at least a portion of the alkyl ester from the second outlet back to the first inlet.
28. The system of claim 25 in which the second subsystem comprises a separator to remove at least a portion of components other than alkyl ester from a first solution output from the second outlet to obtain a second solution that has at least 90% by weight of alkyl ester.
29. The system of claim 28 in which the separator comprises an evaporator.
30. The system of claim 28 in which the separator comprises a liquid-liquid separator.
31. The system of claim 25 in which the first subsystem comprises a separator to remove at least a portion of components other than alkyl ester from a first solution output from the first outlet to obtain a second solution that has a higher concentration of alkyl ester than the first solution.
32. The system of claim 31 in which the separator comprises an evaporator.
33. The system of claim 32 in which the separator comprises a liquid-liquid separator.
34. An apparatus comprising:
a reactor having a pipeline to transmit a mixture comprising a first reactant, a second reactant, an inert solvent, and a reaction product that are in an homogeneous state, a coupler to receive a cartridge having an inlet to receive the mixture from the pipeline, an enzyme to facilitate a reaction between the first and second reactants to generate more reaction product, and an outlet to output the reaction product, including the reaction product received at the inlet and the reaction product generated from the reaction between the first and second reactants;
a separation unit to process the output of the outlet to produce a solution having a higher percentage of the reaction product; and a return mechanism to send at least a portion of the solution back to the pipeline.
35. A system for generating alkyl ester comprising:

a first subsystem including a first reactor having a first pipeline to transmit a first mixture comprising a first reactant, a second reactant, an inert solvent, and alkyl ester that are in a homogeneous state, a first coupler to receive a first cartridge having a first inlet to receive the mixture from the first pipeline, a first enzyme to facilitate a reaction between the first and second reactants to generate alkyl ester, and a first outlet to output the alkyl ester, the solvent, and other components; and a second subsystem including a second reactor having a second pipeline transmit a second mixture comprising additional second reactant, inert solvent, and at least a portion of the alkyl ester and the other components from the first outlet, a second coupler to receive a second cartridge having a second inlet to receive the mixture from the second pipeline, a second enzyme to facilitate a reaction between the second reactant and the other components to generate more alkyl ester, and a second outlet to output the alkyl ester.
36. A system for generating alkyl ester comprising:
a cartridge to receive a mixture comprising a first reactant and a second reactant, the cartridge including an enzyme to facilitate a reaction between the first and second reactants to generate a reaction product, the cartridge having an identifier;
and a controller to control an operation condition of the system based on the identifier on the cartridge.
37. The system of claim 36 in which the reaction product comprises alkyl ester.
38. The system of claim 36 in which the enzyme comprises a lipase.
39. The system of claim 36 in which the controller controls a speed of a pump based on the identifier, in which the speed of the pump affects the speed in which the solution passes through the cartridge.
40. The system of claim 36 in which the controller controls a heater based on the identifier, in which the heater affects a temperature of the solution.
41. The system of claim 36 in which the controller determines when to send a signal indicating that the cartridge needs to be replaced based on the identifier.
42. An apparatus comprising:
a cartridge including a lipase, the cartridge configured to be coupled to an alkyl ester generator that comprises a mixer to mix an oil source and a primary alcohol or a secondary alcohol in an organic solvent to form a solution that is passed through the cartridge, in which the oil source includes a triglyceride and the lipase facilitates a reaction between the triglyceride and the primary alcohol or the secondary alcohol to generate an alkyl ester, in which the solution does not undergo phase separation throughout the reaction and glycerol is produced as a by-product, an evaporator to remove the organic solvent and unreacted primary alcohol or secondary alcohol, a phase separator to separate the alkyl ester from the glycerol, and a second separator to separate the alkyl ester from unreacted oil source.
43. An apparatus comprising:
a cartridge including a lipase, the cartridge configured to be coupled to an alkyl ester generator that comprises a mixer to mix an oil source and a primary alcohol or a secondary alcohol in an organic solvent to form a solution that is passed through the cartridge, in which the oil source includes a carboxylic acid and the lipase facilitates a reaction between the carboxylic acid and the primary alcohol or the secondary alcohol to generate an alkyl ester, in which the solution does not undergo phase separation throughout the reaction and water is produced as a by-product, an evaporator to remove the organic solvent and unreacted primary alcohol or secondary alcohol, and a separator to separate the alkyl ester from unreacted oil source.
44. The apparatus of claim 43 in which the separator comprises a short-path evaporator.
45. An apparatus comprising:
an evaporator having an input to receive a mixture comprising alkyl ester, alcohol, a inert solvent, and glycerol, the evaporator to evaporate the inert solvent and the alcohol to generate a solution including alkyl ester and glycerol, and a separator having an input to receive the solution, the separator to separate the alkyl ester from the glycerol based on liquid-liquid phase separation.
46. An apparatus for producing an alkyl ester, comprising:
a mixer to mix an oil source and a primary alcohol or a secondary alcohol in an organic solvent to form a solution, the oil source including a triglyceride;
a reactor to receive the solution, the reactor including a lipase that facilitates a reaction between the triglyceride and the primary alcohol or the secondary alcohol to generate an alkyl ester, in which glycerol is produced as a by-product;

an evaporator to remove the organic solvent and unreacted primary alcohol or secondary alcohol; and a phase separator to separate the alkyl ester from the glycerol.
47. The apparatus of claim 46 also comprising a carrier, in which the lipase is immobilized on the carrier.
48. The apparatus of claim 46 also comprising a return mechanism to allow at least a portion of the alkyl ester separated by the phase separator to enter the inlet and add to the solution.
49. A method comprising:
inserting a cartridge into an alkyl ester generator, the cartridge having an inlet, and outlet, and an enzyme positioned between the inlet and the outlet;
reading information encoded on the cartridge;
controlling an operation of the alkyl ester generator based on the information.
50. The method of claim 49 in which controlling an operation of the alkyl ester generator comprises controlling at least one of temperature and flow rate of a solution flowing into the inlet of the cartridge.
CA2520163A 2004-09-20 2005-09-16 An apparatus for producing alkyl ester Expired - Fee Related CA2520163C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/945339 2004-09-20
US10/945,339 US7473539B2 (en) 2004-09-20 2004-09-20 Methods for producing alkyl esters

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CA2520163C CA2520163C (en) 2012-01-24

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EP (4) EP1637610B1 (en)
JP (2) JP3892463B2 (en)
KR (2) KR101136890B1 (en)
CN (2) CN100572545C (en)
AR (2) AR050814A1 (en)
AT (2) ATE427997T1 (en)
AU (4) AU2005200356B2 (en)
BR (2) BRPI0500630A (en)
CA (2) CA2493628C (en)
CL (2) CL2009001529A1 (en)
CO (2) CO5630034A1 (en)
DE (2) DE602004020472D1 (en)
DK (2) DK1637610T3 (en)
ES (2) ES2324534T3 (en)
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PE (3) PE20060387A1 (en)
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PT (1) PT1637610E (en)
RU (2) RU2392263C2 (en)
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Families Citing this family (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004019472A1 (en) * 2004-04-22 2005-11-17 Bayer Healthcare Ag phenylacetamides
US7473539B2 (en) * 2004-09-20 2009-01-06 Sunho Biodiesel Corporation Methods for producing alkyl esters
US20080113419A1 (en) * 2005-01-10 2008-05-15 Novozymes A/S Production of Fatty Acid Alkyl Esters by Use of Two Lipolytic Enzymes
CN101180383B (en) * 2005-02-28 2012-01-11 渥太华大学 Apparatus and method for bio-fuel production
US9109170B2 (en) * 2006-02-02 2015-08-18 Reg Biofuels, Llc Biodiesel cold filtration process
US7837891B2 (en) * 2006-02-16 2010-11-23 Nalco Company Fatty acid by-products and methods of using same
MX2008011595A (en) 2006-04-28 2008-09-22 Sk Chemicals Co Ltd Method and apparatus for preparing fatty acid alkyl ester using fatty acid.
GB0617476D0 (en) * 2006-09-06 2006-10-18 Univ Newcastle Improved process for biodiesel production
KR100806517B1 (en) * 2006-11-07 2008-02-21 김학로 Biodiesel manufacturing method with improved low temperature fluidity
UA97127C2 (en) * 2006-12-06 2012-01-10 Бандж Ойлз, Инк. Method and system for the enzymatic treatment of lipid containing feedstock
CL2008002020A1 (en) * 2007-07-12 2008-11-14 Ocean Nutrition Canada Ltd Method of modifying an oil, which comprises hydrolyzing glycerides with a solution of thermomyces lanuginosus lipase, separating the saturated fatty acid fraction from the hydrolyzed glyceride fraction and esterifying the hydrolyzed glycerides in the presence of candida antarctica lipase b; and oil composition.
US20090031698A1 (en) * 2007-07-31 2009-02-05 O'brien & Gere Engineers Inc. Liquid and Solid Biofueled Combined Heat and Renewable Power Plants
CN100548906C (en) * 2007-08-21 2009-10-14 南京大学 The removal method of ammonia nitrogen in a kind of coking chemical waste water
US8076123B2 (en) 2007-10-26 2011-12-13 Oilseeds Biorefinery Corporation Emulsification-free degumming of oil
WO2009065229A1 (en) * 2007-11-23 2009-05-28 University Of Ottawa Technology Transfer And Business Enterprise Biodiesel production using ultra low catalyst concentrations in a membrane reactor
US7790429B2 (en) * 2007-11-28 2010-09-07 Transbiodiesel Ltd. Robust multi-enzyme preparation for the synthesis of fatty acid alkyl esters
BRPI0820588A2 (en) * 2007-12-14 2014-11-04 Kansai Chemical Enginnering Ltd METHOD FOR PRODUCING CONTINUOUS FORM OF A FATTY ACID ESTER AND APPARATUS FOR PRODUCTION OF CONTINUOUS FORM OF FATTY ACID ESTER
US8603198B2 (en) * 2008-06-23 2013-12-10 Cavitation Technologies, Inc. Process for producing biodiesel through lower molecular weight alcohol-targeted cavitation
US9611496B2 (en) 2009-06-15 2017-04-04 Cavitation Technologies, Inc. Processes for extracting carbohydrates from biomass and converting the carbohydrates into biofuels
US9988651B2 (en) 2009-06-15 2018-06-05 Cavitation Technologies, Inc. Processes for increasing bioalcohol yield from biomass
JP4397432B1 (en) * 2009-06-19 2010-01-13 有限会社中部エンザイム Fuel production method and fuel production apparatus
AR080117A1 (en) 2010-03-01 2012-03-14 Trans Bio Diesel Ltd A PROCESS FOR THE ENZYMATIC SYNTHESIS OF ALKYL ESTERS OF FATTY ACIDS
DE102010002809A1 (en) * 2010-03-12 2011-11-17 Evonik Degussa Gmbh Process for the preparation of linear alpha, omega-dicarboxylic acid diesters
US8950199B2 (en) * 2010-03-27 2015-02-10 Perfectly Green Corporation System and method for energy allocation
ES2725848T3 (en) 2010-06-18 2019-09-27 Butamax Tm Advanced Biofuels Extraction solvents derived from oil for the extraction of alcohol in an extractive fermentation
US9040263B2 (en) 2010-07-28 2015-05-26 Butamax Advanced Biofuels Llc Production of alcohol esters and in situ product removal during alcohol fermentation
JP2012021116A (en) * 2010-07-16 2012-02-02 Green Tech Solution:Kk Method for producing biodiesel fuel oil
WO2012106158A2 (en) * 2011-02-01 2012-08-09 Ohana Investment Works Llc Methods and apparatus for controlling moisture in plant oils and liquid biofuels
FR2980377B1 (en) * 2011-09-22 2013-10-04 Total Raffinage Marketing METHOD FOR REGENERATING AN ENZYMATIC CATALYST
WO2013122599A1 (en) * 2012-02-17 2013-08-22 Sunho Biodiesel America Llc Enzymatic production of monoglycerides
US20150353970A1 (en) 2012-12-31 2015-12-10 Trans Bio-Diesel Ltd. Enzymatic transesterification/esterification processing systems and processes employing lipases immobilzed on hydrophobic resins
US9328054B1 (en) 2013-09-27 2016-05-03 Travis Danner Method of alcoholisis of fatty acids and fatty acid gyicerides
WO2015088983A1 (en) 2013-12-09 2015-06-18 Cavitation Technologies, Inc. Processes for extracting carbohydrates from biomass and converting the carbohydrates into biofuels
RU2704822C2 (en) * 2014-03-28 2019-10-31 Роял Корпорэйшн Ко., Лтд. Process and device for production of fuel hydrocarbon oil
WO2016196402A1 (en) 2015-05-29 2016-12-08 Perfectly Green Corporation System, method and computer program product for energy allocation
CN106708129B (en) * 2017-01-16 2018-08-10 徐李 One kind being used for the temperature controlled equipment of beer fermentation

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE754657Q (en) 1965-11-29 1971-01-18 Kenics Corp MIXER APPLIANCE
JPS6071944A (en) * 1983-09-29 1985-04-23 Toshiba Corp Device for measuring enzyme activity
JPS6078587A (en) 1983-10-05 1985-05-04 Lion Corp Preparation of fatty acid ester
JP2554469B2 (en) * 1986-01-16 1996-11-13 日本精化株式会社 Method for producing fatty acid esters
JPS62104589A (en) 1985-10-25 1987-05-15 Meito Sangyo Kk Production of fatty acid ester
FR2596415B1 (en) * 1986-03-26 1988-07-01 Elf Aquitaine PROCESS FOR THE EXECUTION OF ENZYMATIC REACTIONS WITHIN AN ORGANIC SOLVENT
JPH0712313B2 (en) 1986-11-05 1995-02-15 名糖産業株式会社 How to decompose fats and oils
DE3819636A1 (en) 1987-06-16 1988-12-29 Krasnod Stankostroitelnoe Proi Table for a vertical turning and boring mill
FR2617501B1 (en) 1987-07-02 1990-03-16 Elf Aquitaine ENZYMATIC PROCESS CARRIED OUT IN AN ORGANIC SOLVENT
EP0413307A1 (en) 1989-08-15 1991-02-20 Lion Corporation Process for producing saccharide fatty acid monoesters
US5288619A (en) * 1989-12-18 1994-02-22 Kraft General Foods, Inc. Enzymatic method for preparing transesterified oils
JPH0728719B2 (en) * 1991-10-22 1995-04-05 工業技術院長 Continuous ester synthesizer and its continuous synthesis method
US5525126A (en) * 1994-10-31 1996-06-11 Agricultural Utilization Research Institute Process for production of esters for use as a diesel fuel substitute using a non-alkaline catalyst
US5713965A (en) * 1996-04-12 1998-02-03 The United States Of America As Represented By The Secretary Of Agriculture Production of biodiesel, lubricants and fuel and lubricant additives
IL129086A0 (en) 1999-03-22 2000-02-17 Enzymotec Ltd Surfactant-lipase complex immobilized on insoluble matrix
CA2273570A1 (en) * 1999-05-31 2000-11-30 Jfs Envirohealth Ltd. Concentration and purification of polyunsaturated fatty acid esters by distillation-enzymatic transesterification coupling
DE19950593A1 (en) 1999-10-20 2001-05-17 Siegfried Peter Process for obtaining simple fatty acid esters from fat and / or oil of biological origin
JP3853552B2 (en) 1999-12-17 2006-12-06 花王株式会社 Method for producing diglyceride
ATA16992000A (en) * 2000-10-05 2001-12-15 Michael Dr Koncar METHOD FOR PRODUCING FATTY ACID ALKYL ESTERS
DE10122551A1 (en) 2001-05-10 2002-11-21 Zulka Joachim Hans Semi-continuous production of biodegradable fatty acid ester mixtures for use, e.g. as synthetic lubricant, involves enzymatic hydrolysis of vegetable or animal fats and oils in presence of an alcohol
US6398707B1 (en) * 2001-05-31 2002-06-04 Wen-Teng Wu Method of preparing lower alkyl fatty acids esters and in particular biodiesel
CN1279174C (en) * 2002-05-10 2006-10-11 北京化工大学 Fixed lipase catalyzed synthesis of fatty acid low carbon alcohol ester
CN1183238C (en) 2003-03-28 2005-01-05 刘阳 Method of manufacturing vegetable oil methyl aliphate using biological enzyme method
CN1453332A (en) 2003-04-24 2003-11-05 华南理工大学 Biologically catalystic process of converting fat into ester to produce biological diesel oil
US7473539B2 (en) * 2004-09-20 2009-01-06 Sunho Biodiesel Corporation Methods for producing alkyl esters

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