WO2007132775A1 - リパーゼ活性の回復方法 - Google Patents
リパーゼ活性の回復方法 Download PDFInfo
- Publication number
- WO2007132775A1 WO2007132775A1 PCT/JP2007/059751 JP2007059751W WO2007132775A1 WO 2007132775 A1 WO2007132775 A1 WO 2007132775A1 JP 2007059751 W JP2007059751 W JP 2007059751W WO 2007132775 A1 WO2007132775 A1 WO 2007132775A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- lipase
- transesterification
- immobilized
- reaction
- activity
- Prior art date
Links
- 235000019626 lipase activity Nutrition 0.000 title claims abstract description 29
- 238000000034 method Methods 0.000 title claims abstract description 27
- 238000011084 recovery Methods 0.000 title abstract description 4
- 108090001060 Lipase Proteins 0.000 claims abstract description 112
- 102000004882 Lipase Human genes 0.000 claims abstract description 112
- 239000004367 Lipase Substances 0.000 claims abstract description 100
- 235000019421 lipase Nutrition 0.000 claims abstract description 100
- 239000000203 mixture Substances 0.000 claims abstract description 59
- 238000005809 transesterification reaction Methods 0.000 claims abstract description 48
- 239000000843 powder Substances 0.000 claims abstract description 40
- 238000005886 esterification reaction Methods 0.000 claims abstract description 23
- 239000002245 particle Substances 0.000 claims abstract description 21
- DCXXMTOCNZCJGO-UHFFFAOYSA-N tristearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000005406 washing Methods 0.000 claims abstract description 11
- 241000223257 Thermomyces Species 0.000 claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 claims description 23
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 7
- 150000004667 medium chain fatty acids Chemical class 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 4
- 239000001913 cellulose Substances 0.000 claims description 3
- 229920002678 cellulose Polymers 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 20
- 230000032050 esterification Effects 0.000 abstract description 8
- 230000003247 decreasing effect Effects 0.000 abstract description 2
- 244000005700 microbiome Species 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 19
- 235000019198 oils Nutrition 0.000 description 18
- 238000001914 filtration Methods 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- 240000002791 Brassica napus Species 0.000 description 7
- 235000004977 Brassica sinapistrum Nutrition 0.000 description 7
- 235000014113 dietary fatty acids Nutrition 0.000 description 6
- 239000000194 fatty acid Substances 0.000 description 6
- 229930195729 fatty acid Natural products 0.000 description 6
- 238000004817 gas chromatography Methods 0.000 description 6
- 108010048733 Lipozyme Proteins 0.000 description 5
- 239000003925 fat Substances 0.000 description 5
- 235000019197 fats Nutrition 0.000 description 5
- 150000004665 fatty acids Chemical class 0.000 description 5
- FCCDDURTIIUXBY-UHFFFAOYSA-N lipoamide Chemical compound NC(=O)CCCCC1CCSS1 FCCDDURTIIUXBY-UHFFFAOYSA-N 0.000 description 5
- 238000004061 bleaching Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- 150000004668 long chain fatty acids Chemical class 0.000 description 4
- -1 fatty acid esters Chemical class 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 229940093609 tricaprylin Drugs 0.000 description 3
- VLPFTAMPNXLGLX-UHFFFAOYSA-N trioctanoin Chemical compound CCCCCCCC(=O)OCC(OC(=O)CCCCCCC)COC(=O)CCCCCCC VLPFTAMPNXLGLX-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 235000012424 soybean oil Nutrition 0.000 description 2
- 239000003549 soybean oil Substances 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 108090000604 Hydrolases Proteins 0.000 description 1
- 102000004157 Hydrolases Human genes 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 1
- 235000019485 Safflower oil Nutrition 0.000 description 1
- 241001285933 Thermomyces sp. Species 0.000 description 1
- BAECOWNUKCLBPZ-HIUWNOOHSA-N Triolein Natural products O([C@H](OCC(=O)CCCCCCC/C=C\CCCCCCCC)COC(=O)CCCCCCC/C=C\CCCCCCCC)C(=O)CCCCCCC/C=C\CCCCCCCC BAECOWNUKCLBPZ-HIUWNOOHSA-N 0.000 description 1
- PHYFQTYBJUILEZ-UHFFFAOYSA-N Trioleoylglycerol Natural products CCCCCCCCC=CCCCCCCCC(=O)OCC(OC(=O)CCCCCCCC=CCCCCCCCC)COC(=O)CCCCCCCC=CCCCCCCCC PHYFQTYBJUILEZ-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000012051 hydrophobic carrier Substances 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 235000005713 safflower oil Nutrition 0.000 description 1
- 239000003813 safflower oil Substances 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 150000003431 steroids Chemical class 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 1
- 150000003626 triacylglycerols Chemical class 0.000 description 1
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
- 229940117972 triolein Drugs 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/16—Hydrolases (3) acting on ester bonds (3.1)
- C12N9/18—Carboxylic ester hydrolases (3.1.1)
- C12N9/20—Triglyceride splitting, e.g. by means of lipase
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/02—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with glycerol
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N11/00—Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof
- C12N11/14—Enzymes or microbial cells immobilised on or in an inorganic carrier
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/62—Carboxylic acid esters
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
- C12P7/6436—Fatty acid esters
- C12P7/6445—Glycerides
- C12P7/6454—Glycerides by esterification
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
- C12P7/6436—Fatty acid esters
- C12P7/6445—Glycerides
- C12P7/6458—Glycerides by transesterification, e.g. interesterification, ester interchange, alcoholysis or acidolysis
Definitions
- the present invention relates to a method for recovering lipase activity such as various esterification ability and transesterification ability of a specific immobilized lipase or lipase powder composition, and an esterification using the recovered immobilized lipase or lipase powder composition. It is related to the soot reaction and the transesterification of fats and oils.
- Lipases are widely used in esterification reactions of various carboxylic acids such as fatty acids with alcohols such as monoalcohols and polyhydric alcohols, and transesterification reactions between a plurality of carboxylic acid esters. Of these, transesterification is an important technology for the production of various fatty acid esters, sugar esters and steroids, including the modification of animal and vegetable fats and oils.
- lipase an oil and fat hydrolase, as a catalyst for these reactions, it is possible to carry out transesterification under mild conditions at room temperature to about 70 ° C. Compared with conventional chemical reactions, side reactions
- the lipase as a catalyst is a natural product.
- the target product can be produced efficiently due to its substrate specificity and position specificity.
- lipase has conventionally been treated with some kind of carrier such as anion-exchanged resin (Patent Document 1), phenol-adsorbed resin (Patent Document 2), hydrophobic carrier (Patent Document 3), cation-exchanged resin (Patent Document). 4) In general, it is immobilized on chelate rosin (Patent Document 5) or the like and used for esterification or transesterification.
- carrier such as anion-exchanged resin (Patent Document 1), phenol-adsorbed resin (Patent Document 2), hydrophobic carrier (Patent Document 3), cation-exchanged resin (Patent Document).
- ester in the presence or absence of an inert organic solvent, ester is contained so that 90% or more of the dispersed lipase powder particles are maintained at a particle size in the range of 1 to LOO ⁇ m during the transesterification reaction.
- a method of transesterifying by dispersing lipase powder in the raw material It has been proposed (Patent Document 6). It has also been proposed to use enzyme powder obtained by drying an enzyme solution containing phospholipids and fat-soluble vitamins (Patent Document 7).
- the enzyme lipase is expensive, it is recovered after the completion of the reaction and repeatedly used, and is discarded only when the lipase activity is reduced. However, if the lowered lipase activity can be recovered, the use efficiency of the lipase will be improved significantly. From an industrial point of view, development of an effective method for recovering the lipase activity is desired.
- Patent Document 1 Japanese Patent Application Laid-Open No. 60-98984
- Patent Document 2 Japanese Patent Laid-Open No. 61-202688
- Patent Document 3 JP-A-2-138986
- Patent Document 4 JP-A-3-61485
- Patent Document 5 Japanese Patent Laid-Open No. 1-262795
- Patent Document 6 Japanese Patent No. 2668187
- Patent Document 7 Japanese Unexamined Patent Publication No. 2000-106873
- An object of the present invention is to provide a method capable of recovering reduced lipase activity.
- Another object of the present invention is to provide an esterification method and a transesterification method using an immobilized lipase or lipase powder composition having recovered lipase activity.
- the present invention relates to a lipase powder composition
- a lipase powder composition comprising a specific immobilized lipase or a pulverized product of the immobilized lipase in combination with a filter aid. This is based on the knowledge that lipase activity can be restored.
- the present invention relates to a lipase derived from Thermomyces genus immobilized on a carrier or a lipase derived from Thermomyces genus immobilized on a carrier and having an average particle diameter of 1 ⁇ m or more and less than 300 m, and a filter aid.
- a method for recovering lipase activity characterized in that a lipase powder composition containing an agent is used for esterification reaction or transesterification and then washed with triacylglycerol.
- the present invention also provides a lipase derived from Thermomyces genus immobilized on a carrier or a lipase derived from Thermomyces genus immobilized on a carrier and having an average particle diameter of 1 ⁇ m or more and less than 300 ⁇ m and a filter aid.
- the lipase powder composition containing the agent is used in the esterification reaction or transesterification reaction, it is separated from the reaction system, washed with triacylglycerol to recover the lipase activity, and then this immobilized lipase or lipase is recovered.
- a method for esterification reaction or transesterification characterized by carrying out esterification reaction or transesterification reaction using a powder composition.
- the lipase used in the present invention is a lipase derived from Thermomyces sp. And immobilized on a carrier, preferably a silica carrier.
- a carrier preferably a silica carrier.
- the lipase can be used as it is, or the lipase pulverized to an average particle size of 1 ⁇ m or more and less than 300 m can be used.
- the average particle size of the lipase immobilized on a silica carrier is preferably about 300 to 1000 ⁇ m.
- Such an immobilized lipase can be obtained as, for example, Lipozyme TL-IM from Novozymes A / S.
- a pulverizer a mortar, a shear friction pulverizer, a cutter pulverizer, a stone mill (my colloider, masco mouth ider), a coffee mill, a power mill, a pin mill, an impact pulverizer (a non-mer mill, a ball mill), a roll Pulverizer, airflow pulverizer, homogenizer, and ultrasonic crusher.
- the lipase targeted in the present invention is the above pulverized product, it is preferably used in combination with a filter aid.
- filter aids include inorganic filter aids such as celite and organic filter aids such as fibers such as cellulose and pulverized products thereof. Among them, organic filter aids, especially organic polymer filter aids are preferred, but cellulose and the like are preferred. Nippon Paper Chemicals Co., Ltd. has been marketed under the trade name KC Flock, etc. It can be given as a thing.
- the filter aid is also preferably in the form of a powder and preferably has an average particle size of 10 to 90 m.
- the mass ratio of the lipase pulverized product to the filter aid is preferably 1/10 to: LO / 1, particularly preferably 1/7 to 2/1.
- the above-mentioned immobilized lipase lipase powder composition used in the present invention is a force S that can be used as it is in an ester exchange reaction or esterification reaction of fats and oils. Then, by collecting it, it can be purified and at the same time the lipase activity can be improved.
- long-chain fatty acid triglyceride and the medium-chain fatty acid triglyceride used here those described in the section of washing the immobilized lipase lipase powder composition described later are preferably used.
- the mass ratio of long-chain fatty acid triglycerides and medium-chain fatty acid triglycerides is preferably 2 to 100 times the total mass of lipase, which is preferably used in a ratio of 95: 5 to 50:50. It is preferable to contact triglycerides.
- an oil esterification reaction is performed in the presence of the immobilized lipase lipase powder composition, and then the immobilized lipase lipase powder composition is recovered. It is preferable to recycle.
- the lipase powder composition described above has improved lipase activity and improved ease of use (operability) in esterification reactions and transesterification reactions, and can be recycled for use in these reactions. Therefore, it can be suitably used for the modification of fats and oils by transesterification of fats and oils on an industrial scale.
- the lipase activity is recovered, and the lipase powder composition described above has improved lipase activity and use. Ease of use (operability) can be used for a long period of time.
- the lipase powder composition in which the immobilized lipase lipase activity targeted in the present invention is reduced it is possible to target those that have decreased even a little with respect to the initial activity, From an industrial point of view, it is preferable to target those whose initial activity (100%) has dropped to 70-50%.
- the triacylglycerol used for washing the immobilized lipase lipase powder composition is preferably liquid at room temperature.
- the long-chain fatty acid triglyceride used here is preferably a triglyceride having 14 to 24 carbon atoms in the constituent fatty acid, and particularly a group power consisting of rapeseed oil, soybean oil, castor oil, safflower oil, and corn oil is also selected. Preference is given to vegetable oil.
- the medium-chain fatty acid triglyceride is preferably a triglyceride having from 12 to 12 carbon atoms of the constituent fatty acid.
- a fatty acid triglyceride can be produced by a known production method, or a commercially available product can be used.
- the long chain fatty acid triglyceride and the medium chain fatty acid triglyceride are used in a mass ratio of 95: 5 to 50:50, preferably 2 to 100 times the total mass of lipase. More preferably, the triglyceride having a mass of 5 to 50 times is contacted.
- triacylglycerol used for washing is preferably a raw material oil for transesterification.
- the washing is performed so that the lipase in the immobilized lipase lipase powder composition is sufficiently in contact with the above triacyl darrol. Specifically, the washing is performed after the esterification reaction or the transesterification reaction.
- the immobilized lipase lipase powder composition is dispersed by stirring in triacylglycerol and then separated by triacylglycerol force.
- stirring is preferably performed at 10 to 45 ° C., particularly preferably at room temperature, preferably 2 hours or more, more preferably 10 hours or more, and particularly preferably 12 hours to 48 hours. If desired, it may be performed for 48 hours or longer.
- the stirrer used for stirring is not particularly limited, but a blade stirrer, a magnetic stirrer, a three-one motor, or the like is preferably used.
- the lipase in the immobilized lipase lipase powder composition is sufficiently brought into contact with triacyldaricerol, and then filtered by a conventional method to separate the fixed lipase lipase powder composition from triacylglycerol. Used for esterification and transesterification.
- the lipase activity is reduced by using the lipase in various reactions.
- the lipase activity can be recovered by the method of the present invention. Since the lifetime can be extended and the cost of a product manufactured using lipase can be reduced, the present invention has a great merit from an industrial point of view.
- Lipozyme TL-IM average particle size 800 ⁇ m
- IKg manufactured by Novozymes
- a / S was pulverized at 17600 rpm using a pin mill (fine impact mill 100 UPZ) manufactured by Hosokawa Micron.
- the pulverized lipase particle size was measured using a particle size distribution analyzer LA-500 manufactured by Horiba, the average particle size was 13.8 ⁇ m.
- 1 kg of cellulose powder (Nippon Paper Chemicals: average particle size 30 ⁇ m) was added as a filter aid to make a lipase powder composition.
- a lipase composition was added to an oil in which triolein and tricaprylin were mixed at a ratio of 1: 1 (w) and reacted at 60 ° C.
- a sample of 101 was sampled over time, diluted with 1.5 ml of hexane, and the solution obtained by filtering the lipase composition was used as a sample for gas chromatography (GC).
- GC gas chromatography
- Analyzed by GC column temperature: initial 1 50 ° C, temperature rise: 15 ° C / min, final 370 ° C.
- C24 indicates tricaprylin
- C34 indicates that one fatty acid of tricaprylin is replaced by oleic acid
- area is the area of those areas.
- the lipase activity was expressed as relative activity when the k value of Lipozyme TL-IM was 100.
- the lipase composition having a relative activity reduced to about 60% in (3) above is collected by filtration, and the collected lipase composition is rapeseed decolorized oil (Nisshin Oilio Group, Inc.) 18 g) and 2 g of ODO (Nisshin Oillio Group Co., Ltd.) were added and stirred at room temperature for 24 hours using a magnetic stirrer. After recovering the lipase yarn and the product by filtration, the transesterification was repeated again in the same manner as in (3) above.
- Figure 2 shows the results of confirming the change in the reaction rate with the relative ratio.
- the lipase composition with reduced activity can be recovered by stirring and washing so that the lipase activity is restored to the original 100%, and the lipase composition can be recycled and used several times.
- Rapeseed bleaching oil (Nisshin Oillio Group Co., Ltd.) 85g, and ODO (Nisshin Oillio Doop Co., Ltd.) 15g Lipozyme TL-IM (immobilized lipase: Novozymes A / S) 5 quality
- the transesterification was carried out by adding 19% and stirring at 60 ° C for 19 hours. The transesterification rate was obtained over time, and the progress of the reaction was confirmed.
- the transesterification reaction was determined by analyzing the glyceride composition using gas chromatography and calculating the ratio of the transesterification product in the measurement sample.
- FIG. 1 shows a decrease in ester exchange activity over time when a transesterification reaction is performed using a lipase powder composition (Example 1 (3)).
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Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2007800260242A CN101490254B (zh) | 2006-05-11 | 2007-05-11 | 脂肪酶活性的恢复方法 |
EP07743186A EP2019135B1 (en) | 2006-05-11 | 2007-05-11 | Method for recovery of lipase activity |
ES07743186T ES2402902T3 (es) | 2006-05-11 | 2007-05-11 | Método de recuperación de la actividad de la lipasa |
CA2652076A CA2652076C (en) | 2006-05-11 | 2007-05-11 | Method of recovering lipase activity |
DK07743186.4T DK2019135T3 (da) | 2006-05-11 | 2007-05-11 | Fremgangsmåde til genvinding af lipaseaktivitet |
AU2007250913A AU2007250913B2 (en) | 2006-05-11 | 2007-05-11 | Method of recovering lipase activity |
US12/266,617 US7923224B2 (en) | 2006-05-11 | 2008-11-07 | Method of recovering lipase activity |
NO20085072A NO20085072L (no) | 2006-05-11 | 2008-12-04 | Fremgangsmate for gjenvinning av lipaseaktivitet |
HK09111004.2A HK1131189A1 (en) | 2006-05-11 | 2009-11-25 | Method for recovery of lipase activity |
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JP2006-132639 | 2006-05-11 | ||
JP2006132639A JP4917349B2 (ja) | 2006-05-11 | 2006-05-11 | リパーゼ活性の回復方法 |
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US12/266,617 Continuation US7923224B2 (en) | 2006-05-11 | 2008-11-07 | Method of recovering lipase activity |
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WO2007132775A1 true WO2007132775A1 (ja) | 2007-11-22 |
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US (1) | US7923224B2 (ja) |
EP (1) | EP2019135B1 (ja) |
JP (1) | JP4917349B2 (ja) |
KR (1) | KR20090010048A (ja) |
CN (1) | CN101490254B (ja) |
AU (1) | AU2007250913B2 (ja) |
CA (1) | CA2652076C (ja) |
DK (1) | DK2019135T3 (ja) |
ES (1) | ES2402902T3 (ja) |
HK (1) | HK1131189A1 (ja) |
MY (1) | MY145036A (ja) |
NO (1) | NO20085072L (ja) |
RU (1) | RU2465329C2 (ja) |
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Cited By (4)
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WO2010110424A1 (ja) * | 2009-03-27 | 2010-09-30 | 日清オイリオグループ株式会社 | リパーゼ粉末組成物の製造方法 |
WO2013018859A1 (ja) * | 2011-08-02 | 2013-02-07 | 日清オイリオグループ株式会社 | エステル交換油の製造方法 |
JP2013039109A (ja) * | 2011-08-19 | 2013-02-28 | Nisshin Oillio Group Ltd | リパーゼ活性の回復方法 |
JP2019054738A (ja) * | 2017-09-20 | 2019-04-11 | 花王株式会社 | 脂肪酸類の製造方法 |
Families Citing this family (3)
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JP5586855B2 (ja) * | 2009-02-12 | 2014-09-10 | 花王株式会社 | モノアシルグリセロール高含有油脂の製造方法 |
JP2012206084A (ja) * | 2011-03-30 | 2012-10-25 | Cci Corp | 油脂含有排水の処理方法およびその排水処理材 |
RU2020120682A (ru) * | 2017-11-24 | 2021-12-24 | Новозимс А/С | Мелкие частицы на основе фермента для переэтерификации |
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- 2007-05-09 TW TW096116396A patent/TWI398521B/zh not_active IP Right Cessation
- 2007-05-11 EP EP07743186A patent/EP2019135B1/en active Active
- 2007-05-11 MY MYPI20084498A patent/MY145036A/en unknown
- 2007-05-11 WO PCT/JP2007/059751 patent/WO2007132775A1/ja active Application Filing
- 2007-05-11 CN CN2007800260242A patent/CN101490254B/zh active Active
- 2007-05-11 CA CA2652076A patent/CA2652076C/en not_active Expired - Fee Related
- 2007-05-11 KR KR1020087027503A patent/KR20090010048A/ko not_active Application Discontinuation
- 2007-05-11 RU RU2008148843/10A patent/RU2465329C2/ru not_active IP Right Cessation
- 2007-05-11 ES ES07743186T patent/ES2402902T3/es active Active
- 2007-05-11 AU AU2007250913A patent/AU2007250913B2/en not_active Ceased
- 2007-05-11 DK DK07743186.4T patent/DK2019135T3/da active
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2008
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- 2008-12-04 NO NO20085072A patent/NO20085072L/no unknown
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WO2010110424A1 (ja) * | 2009-03-27 | 2010-09-30 | 日清オイリオグループ株式会社 | リパーゼ粉末組成物の製造方法 |
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CN102449146A (zh) * | 2009-03-27 | 2012-05-09 | 日清奥利友集团株式会社 | 脂肪酶粉末组合物的制造方法 |
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JP2013032439A (ja) * | 2011-08-02 | 2013-02-14 | Nisshin Oillio Group Ltd | エステル交換油の製造方法 |
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JP2019054738A (ja) * | 2017-09-20 | 2019-04-11 | 花王株式会社 | 脂肪酸類の製造方法 |
JP6990076B2 (ja) | 2017-09-20 | 2022-02-03 | 花王株式会社 | 脂肪酸類の製造方法 |
Also Published As
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AU2007250913B2 (en) | 2012-06-28 |
EP2019135A1 (en) | 2009-01-28 |
KR20090010048A (ko) | 2009-01-28 |
US7923224B2 (en) | 2011-04-12 |
TWI398521B (zh) | 2013-06-11 |
TW200813229A (en) | 2008-03-16 |
CA2652076A1 (en) | 2007-11-22 |
US20090075349A1 (en) | 2009-03-19 |
MY145036A (en) | 2011-12-15 |
NO20085072L (no) | 2008-12-05 |
JP4917349B2 (ja) | 2012-04-18 |
RU2008148843A (ru) | 2010-06-20 |
DK2019135T3 (da) | 2013-04-15 |
JP2007300855A (ja) | 2007-11-22 |
EP2019135A4 (en) | 2009-11-11 |
EP2019135B1 (en) | 2013-03-06 |
AU2007250913A1 (en) | 2007-11-22 |
RU2465329C2 (ru) | 2012-10-27 |
HK1131189A1 (en) | 2010-01-15 |
ES2402902T3 (es) | 2013-05-10 |
CA2652076C (en) | 2015-01-06 |
CN101490254A (zh) | 2009-07-22 |
CN101490254B (zh) | 2011-10-05 |
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