WO2019155790A1 - ランダムエステル交換リパーゼ - Google Patents
ランダムエステル交換リパーゼ Download PDFInfo
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- WO2019155790A1 WO2019155790A1 PCT/JP2018/048378 JP2018048378W WO2019155790A1 WO 2019155790 A1 WO2019155790 A1 WO 2019155790A1 JP 2018048378 W JP2018048378 W JP 2018048378W WO 2019155790 A1 WO2019155790 A1 WO 2019155790A1
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- lipase
- amino acid
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- acid sequence
- oils
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- 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
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- 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
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- 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
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y301/00—Hydrolases acting on ester bonds (3.1)
- C12Y301/01—Carboxylic ester hydrolases (3.1.1)
- C12Y301/01003—Triacylglycerol lipase (3.1.1.3)
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/645—Fungi ; Processes using fungi
- C12R2001/72—Candida
Definitions
- the present invention relates to a random transesterification lipase and its use.
- This application claims priority based on Japanese Patent Application No. 2018-022487 filed on Feb. 9, 2018, the entire contents of which are incorporated by reference.
- the transesterification reaction of fats and oils is an effective method for modifying the physical properties of oils and fats (melting point, crystallinity, heat resistance, etc.), and can be roughly divided into two types: chemical transesterification and enzymatic transesterification (for example, (See Non-Patent Documents 1 and 2).
- Chemical transesterification has many problems such as high environmental impact and poor work safety.
- due to concerns about the health risks of trans fatty acids the production of transesterified oils and fats as an alternative to partial hydrogenation that causes trans fatty acids has attracted attention, and the demand for enzymatic random transesterification has increased.
- lipases derived from Candida, Alcaligenes, Pseudomonas, Humicola (trade name: Novozyme, Lipozyme TL IM), etc. can be used.
- the present applicant has reported a novel lipase derived from a microorganism of the genus Geobacillus that exhibits random transesterification ability.
- the present inventors conducted a large-scale screening for about 1,500 strains of microorganisms (bacteria, yeast, filamentous fungi, actinomycetes, etc.).
- microorganisms bacteria, yeast, filamentous fungi, actinomycetes, etc.
- the inventors succeeded in identifying the amino acid sequence of the enzyme and the base sequence of the gene encoding the enzyme. The following invention is based on these results.
- a lipase having the following enzyme chemical properties (1) Action: catalyze random transesterification, (2) Molecular weight: The molecular weight without the N-type sugar chain is about 36 kDa (by SDS-PAGE), (3) Temperature stability in fats and oils: Stable at 60 ° C or less (by evaluation using tricaprylin and methyl stearate as substrates and methyl caprylate production as an index), (4) Reactivity in fats and oils: When reacted at 40 to 80 ° C., the highest reactivity is shown at 80 ° C. (based on evaluation using cocoa butter as a substrate and the amount of tripalmitin produced as an index).
- An enzyme agent comprising the lipase according to any one of [1] to [7].
- a random transesterification method for fats and oils comprising the step of allowing the lipase according to any one of [1] to [7] to act on the fats and oils.
- a method for producing a lipase for random transesterification comprising the following steps (1) and (2): (1) culturing Candida parargosa; (2) A step of recovering lipase from the culture solution and / or the cells after culturing. [11] The production method according to [10], wherein Candida parargosa is NBRC 0966 strain. [12] A method for producing a random transesterified oil or fat, comprising the step of causing the lipase according to any one of [1] to [7] to act on the oil or fat.
- a lipase gene comprising any DNA selected from the group consisting of the following (a) to (c): (a) a DNA encoding the amino acid sequence of SEQ ID NO: 2 or an amino acid sequence equivalent to the amino acid sequence; (b) DNA consisting of the nucleotide sequence of SEQ ID NO: 4 or 5; (c) DNA encoding a protein having a base sequence equivalent to the base sequence of SEQ ID NO: 4 or 5 and having random transesterification activity. [14] A recombinant DNA comprising the lipase gene according to [13]. [15] A microorganism having the recombinant DNA according to [14].
- a method for producing lipase comprising the following steps (i) and (ii): (i) culturing the microorganism according to [15] under conditions under which a protein encoded by the gene is produced; (ii) recovering the produced protein.
- PH stability of a novel lipase derived from Candida pararugosa NBRC 0966 Optimum pH of a novel lipase derived from Candida parargosa NBRCNB0966. Temperature stability of a novel lipase derived from Candida parargosa NBRCNB0966. After treatment for 1 hour at each temperature in tricaprylin, the amount of methyl caprylate produced by the reaction using tricaprylin and methyl stearate as substrates was compared. Reactivity of a novel lipase derived from Candida paraargosa NBRC 0966. Comparison was made with the amount of tolpalmitin (PPP) produced after 8 hours of reaction at each reaction temperature. Hydrophobic chromatography purification chart.
- PPP tolpalmitin
- A SDS-PAGE result of the purified fraction by hydrophobic chromatography.
- B End-Hf treatment result of active main peak fraction.
- Lane M Molecular weight marker (manufactured by GE Healthcare).
- Lane 1 Endo-Hf
- Lane 2 Active main peak fraction after Endo-Hf treatment
- Lane 3 Active main peak fraction not treated with Endo-Hf. Change in the amount of tripalmitin produced by the purified enzyme over time. Change over time in the amount of tripalmitin produced by the recombinant enzyme.
- isolated is used herein interchangeably with “purified”.
- isolated is used to distinguish it from its natural state, ie, one that exists in nature. An artificial operation of isolation results in an “isolated state” that is different from the natural state. What has been isolated is clearly and critically different from the natural product itself.
- the purity of the isolated enzyme is not particularly limited. However, if application to a use requiring high purity is planned, it is preferable that the purity of the isolated enzyme is high.
- the 1st aspect of this invention is related with the novel lipase which the present inventors succeeded in acquisition and identification, and found the usefulness.
- the lipase of the present invention (hereinafter also referred to as “the present enzyme”) is characterized by having the following enzymatic chemical properties.
- This enzyme is a lipase and catalyzes a random transesterification reaction.
- the random transesterification activity can be evaluated by a method using cocoa butter (cocoa butter) as a substrate (“Random transesterification activity measurement method” described later).
- Cocoa butter contains oleic acid, palmitic acid, stearic acid and the like as constituent fatty acids, and is mainly composed of triglyceride with oleic acid bonded to the 2-position. Therefore, tolpalmitin (PPP) in which palmitic acid is bonded to all of the 1st, 2nd and 3rd positions is produced only by random transesterification (the 1st or 3rd position palmitic acid is converted to the 2nd oleic acid). It is necessary to exchange, and when the reaction is carried out with lipase specific to the 1st and 3rd positions, triglycerides with palmitic acid inserted in the 2nd position are not generated).
- PPP tolpalmitin
- the random transesterification activity can be evaluated using the tripalmitin production amount as an index. It can be said that the random transesterification reaction is catalyzed if the reaction rate of tripalmitin (C48) is increased by the reaction when evaluated by the random transesterification activity measurement method described later.
- the degree of increase is not particularly limited, but preferably ⁇ PPP (%) is 0.01 or more, more preferably ⁇ PPP (%) is 0.03 or more, and further preferably ⁇ PPP (%) is 0.05 or more.
- this enzyme contains a sugar chain (ie, it is a glycoprotein) and does not contain the N-type sugar chain after removal of the N-type sugar chain.
- the molecular weight of this enzyme is about 36 kDa (molecular weight measured by SDS-PAGE).
- Temperature stability in fats and oils can be evaluated by a method (details will be described later) using tricaprylin and methyl stearate as substrates and the amount of methyl caprylate produced as an index. it can.
- the enzyme of the present invention maintains 90% or more activity at 60 ° C. or lower when treated in tricaprylin for 1 hour.
- the enzyme having such excellent temperature stability is suitable for food applications that require treatment at a relatively high temperature (for example, processing of fats and oils having a high melting point).
- the enzyme can be further characterized by the following enzymatic chemistry (5) and (6).
- pH stability This enzyme shows stable activity at pH 3-7. For example, if the pH of the enzyme solution to be treated is in the range of 3 to 7, it shows 80% or more of the maximum activity after treatment at 30 ° C. for 1 hour.
- the pH stability is, for example, in glycine-hydrochloric acid buffer in the pH range of pH 2 to 3, in citrate buffer in the pH range of pH 3 to 6, in phosphate buffer in the pH range of pH 6 to 8. Judgment is made based on the measurement results in Tris-hydrochloric acid buffer in the pH range of ⁇ 9, and in sodium carbonate buffer in the pH range of pH 9-11.
- Optimum pH The optimum pH of this enzyme is 6. The optimum pH is determined based on, for example, the results measured in Briton Robinson buffer (pH 2 to 9).
- This enzyme can be further characterized by its origin, ie, “Candida pararugosa”.
- “Derived from Candida parargosa” means a lipase produced by a microorganism (can be a wild strain or a mutant strain) classified as Candida parargosa, or Candida parargosa (even a wild strain). It may be a lipase obtained by genetic engineering techniques using a lipase gene (which may be a mutant). Therefore, recombinants produced by a host microorganism into which a lipase gene obtained from Candida paraargosa (or a gene modified from the gene) or a gene having a base sequence equivalent thereto is also a lipase derived from Candida parargosa.
- Candida parargosa from which the present enzyme is derived is referred to as the origin of the present enzyme.
- the microorganisms (Candida paraargosa, host microorganism) used for producing this enzyme are called producing bacteria.
- NBRC 0966 A specific example of Candida paralugossa is NBRC 0966.
- the NBRC 0966 strain is a strain (published as NBRC 0966 in the NBRC Culture catalog) stored in the National Institute of Technology and Evaluation (2-5-8, Kazusa Kamashichi, Kisarazu City, Chiba Prefecture). It can be obtained through procedures.
- the enzyme As a result of analyzing the amino acid sequence of the purified enzyme (lipase) derived from NBRC 0966 strain, it was revealed that the N-terminal amino acid sequence was VTDEPLENVPGILSHPTI (SEQ ID NO: 1). Based on this fact, the enzyme can be further characterized by the N-terminal amino acid sequence.
- This enzyme has the feature that the amino acid sequence of SEQ ID NO: 1 or an amino acid sequence equivalent to the amino acid sequence is included at the N-terminus.
- one embodiment of the present invention is characterized by comprising a protein having the amino acid sequence represented by SEQ ID NO: 2.
- the modified protein may have a function equivalent to that of the protein before modification. That is, the modification of the amino acid sequence does not substantially affect the function of the protein, and the function of the protein may be maintained before and after the modification.
- the present invention provides a protein (hereinafter, also referred to as “equivalent protein”) having an amino acid sequence equivalent to the amino acid sequence shown in SEQ ID NO: 2 and having random transesterification activity.
- the “equivalent amino acid sequence” in this specification is partly different from the reference sequence (the amino acid sequence of SEQ ID NO: 1 or the amino acid sequence of SEQ ID NO: 2).
- the degree of activity is not particularly limited as long as it can function as a random transesterified lipase. However, it is preferably the same level or higher than the enzyme having a reference sequence at the N-terminus.
- an enzyme having an equivalent amino acid sequence catalyzes a random transesterification reaction.
- the degree of activity is not particularly limited as long as it can function as a random transesterified lipase. However, it is preferably about the same as or higher than the enzyme having the reference amino acid sequence (SEQ ID NO: 2).
- the “partial difference in amino acid sequence” when the amino acid sequence of SEQ ID NO: 1 is a standard is typically 1 to several (upper limit is, for example, 2, 3, 4) constituting the amino acid sequence. ) Amino acid deletions, substitutions, or additions, insertions, or combinations of 1 to several amino acids (upper limit is 2, 3 or 4), for example. That means.
- the difference in the amino acid sequence here is allowed as long as the random transesterification ability is maintained (there may be some variation in activity). As long as this condition is satisfied, the positions where the amino acid sequences are different are not particularly limited, and differences may occur at a plurality of positions.
- the equivalent amino acid sequence is, for example, about 75% or more, preferably about 80% or more, more preferably about 85% or more, even more preferably about 90% or more when the amino acid sequence of SEQ ID NO: 1 is used as a reference. Most preferably it has about 95% or more identity.
- the difference in amino acid sequence may occur at a plurality of positions.
- the “partial difference in amino acid sequence” when the amino acid sequence of SEQ ID NO: 2 is a standard is typically 1 to several (upper limit is, for example, 2, 3, 4) constituting the amino acid sequence. 5, 6, 7, 8, 9 amino acid deletions, substitutions, or 1 to several (upper limit is 2, 3, 4, 5, 6, 7) , 8 or 9) amino acid addition, insertion, or a combination thereof has caused a mutation (change) in the amino acid sequence.
- the difference in the amino acid sequence here is allowed as long as the random transesterification ability is maintained (there may be some variation in activity). As long as this condition is satisfied, the positions where the amino acid sequences are different are not particularly limited, and differences may occur at a plurality of positions.
- the ⁇ plurality '' here is, for example, a number corresponding to less than about 30% of all amino acids, a number corresponding to less than about 20%, a number corresponding to less than about 15%, or a number corresponding to less than about 10%, Preferably it is a number corresponding to less than about 5%, more preferably a number corresponding to less than about 3%, even more preferably a number corresponding to less than about 2%, most preferably less than about 1%. It is a corresponding number. That is, the equivalent protein has a reference amino acid sequence of, for example, about 70% or more, about 80% or more, about 85% or more, or about 90% or more, preferably about 95% or more, more preferably about 97% or more, even more preferably. Has an identity of about 98% or more, most preferably about 99% or more (higher percentage of identity is preferred). The difference in amino acid sequence may occur at a plurality of positions.
- an equivalent amino acid sequence is obtained by conservative amino acid substitution occurring at an amino acid residue that is not essential for random transesterification ability.
- conservative amino acid substitution refers to substitution of a certain amino acid residue with an amino acid residue having a side chain having the same properties.
- a basic side chain eg lysine, arginine, histidine
- an acidic side chain eg aspartic acid, glutamic acid
- an uncharged polar side chain eg glycine, asparagine, glutamine, serine, threonine, tyrosine
- Cysteine eg alanine, valine, leucine, isoleucine, proline, phenylalanine, methionine, tryptophan
- ⁇ -branched side chains eg threonine, valine, isoleucine
- aromatic side chains eg tyrosine, phenylalanine, Like tryptophan and histidine.
- a conservative amino acid substitution is preferably a substitution between amino acid residues within the same family.
- the identity (%) of two amino acid sequences or two nucleic acids can be determined by the following procedure, for example.
- two sequences are aligned for optimal comparison (eg, a gap may be introduced into the first sequence to optimize alignment with the second sequence).
- a molecule amino acid residue or nucleotide
- identity (%) number of identical positions / total number of positions ⁇ 100)
- optimal alignment Take into account the number and size of gaps required for conversion.
- Gapped BLAST described in Altschul et al. (1997) Amino Acids Research 25 (17): 3389-3402 can be used.
- gap weight 12, 10, 8, 6, or 4
- the enzyme may be part of a larger protein (eg, a fusion protein).
- a larger protein eg, a fusion protein
- sequences added in the fusion protein include sequences useful for purification, such as multiple histidine residues, and additional sequences that ensure stability during recombinant production.
- the present enzyme having the above amino acid sequence can be easily prepared by a genetic engineering technique. For example, it can be prepared by transforming a suitable host cell (for example, E. coli) with DNA encoding the present enzyme and recovering the protein expressed in the transformant. The recovered protein is appropriately purified according to the purpose. Thus, if this enzyme is obtained as a recombinant protein, various modifications are possible. For example, if a DNA encoding this enzyme and another appropriate DNA are inserted into the same vector and a recombinant protein is produced using the vector, the peptide consists of a recombinant protein linked to any peptide or protein. This enzyme can be obtained.
- a suitable host cell for example, E. coli
- modification may be performed so that addition of sugar chain and / or lipid, or processing of N-terminal or C-terminal may occur.
- modification as described above, extraction of recombinant protein, simplification of purification, addition of biological function, and the like are possible.
- the enzyme is provided, for example, in the form of an enzyme agent.
- the enzyme agent may contain excipients, buffers, suspension agents, stabilizers, preservatives, preservatives, physiological saline and the like.
- the degree of purification of the enzyme as an active ingredient is not particularly limited. That is, it may be a crude enzyme or a purified enzyme.
- the excipient lactose, sorbitol, D-mannitol, maltodextrin, sucrose and the like can be used. Phosphate, citrate, acetate, etc. can be used as the buffer.
- the stabilizer propylene glycol, ascorbic acid or the like can be used.
- phenol benzalkonium chloride
- benzyl alcohol chlorobutanol
- methylparaben and the like
- benzalkonium chloride paraoxybenzoic acid, chlorobutanol and the like can be used.
- Nucleic acid encoding the present enzyme etc.
- the second aspect of the present invention provides a nucleic acid related to the present enzyme. That is, a gene encoding the enzyme, a nucleic acid that can be used as a probe for identifying the nucleic acid encoding the enzyme, and a nucleic acid that can be used as a primer for amplifying or mutating the nucleic acid encoding the enzyme Is provided.
- the gene encoding this enzyme is typically used for the preparation of this enzyme. According to a genetic engineering preparation method using a gene encoding this enzyme, it is possible to obtain the enzyme in a more homogeneous state. This method can also be said to be a suitable method when preparing a large amount of the present enzyme.
- the use of the gene encoding this enzyme is not limited to the preparation of this enzyme.
- the nucleic acid can be used as an experimental tool for elucidating the mechanism of action of the enzyme, or as a tool for designing or preparing a mutant of the enzyme.
- the “gene encoding the enzyme” refers to a nucleic acid from which the enzyme is obtained when it is expressed, not to mention a nucleic acid having a base sequence corresponding to the amino acid sequence of the enzyme. Also included are nucleic acids obtained by adding sequences that do not encode amino acid sequences to such nucleic acids. Codon degeneracy is also considered. For a nucleic acid having a base sequence that does not include a start codon, the enzyme can be obtained by expressing the nucleic acid after adding a start codon or a signal peptide including the start codon.
- sequences of genes encoding this enzyme are SEQ ID NO: 4 (cDNA sequence encoding mature sequence (amino acid sequence of SEQ ID NO: 2), not including signal sequence), SEQ ID NO: 5 (including signal peptide) It is a cDNA sequence encoding the sequence (amino acid sequence of SEQ ID NO: 3) and includes a signal sequence).
- the nucleic acid of the present invention is isolated by using standard genetic engineering techniques, molecular biological techniques, biochemical techniques, etc. with reference to the sequence information disclosed in this specification or the attached sequence listing. Can be prepared.
- a nucleic acid (hereinafter referred to as an “equivalent nucleic acid”) having a base sequence different from that of a protein encoded by the enzyme that is equivalent in function to the base sequence of the gene encoding the enzyme.
- a base sequence defining an equivalent nucleic acid is also referred to as an “equivalent base sequence”.
- an enzyme characteristic of this enzyme comprising a base sequence including substitution, deletion, insertion, addition, or inversion of one or more bases based on the base sequence of the nucleic acid encoding this enzyme
- a DNA encoding a protein having activity ie, random transesterification activity
- Base substitution or deletion may occur at a plurality of sites.
- plurality refers to, for example, 2 to 40 bases, preferably 2 to 20 bases, more preferably 2 to 10 bases, although it depends on the position and type of amino acid residues in the three-dimensional structure of the protein encoded by the nucleic acid It is.
- the equivalent nucleic acid is, for example, 60% or more, preferably 70% or more, more preferably 80% or more, and still more preferably 85% with respect to the base sequence (SEQ ID NO: 4 or SEQ ID NO: 5). More preferably, it has an identity of about 90% or more, still more preferably 95% or more, and most preferably 99% or more.
- Such equivalent nucleic acids include, for example, restriction enzyme treatment, treatment with exonuclease and DNA ligase, position-directed mutagenesis (MolecularMCloning, lonThird Edition, Chapter 13, Cold Spring Harbor Laboratory Press, New York) It can be obtained by introducing mutations by mutation introduction methods (Molecular Cloning, Third Edition, Chapter 13, Cold Spring Harbor Laboratory Press, New York).
- the equivalent nucleic acid can also be obtained by other methods such as ultraviolet irradiation.
- Another aspect of the present invention relates to a nucleic acid having a base sequence complementary to the base sequence of the gene encoding this enzyme. Still another embodiment of the present invention is at least about 60%, 70%, 80%, 90%, 95%, 99% of the base sequence of the gene encoding the enzyme of the present invention, or a base sequence complementary thereto. %, 99.9% nucleic acid having the same base sequence is provided.
- Still another embodiment of the present invention relates to a nucleic acid having a base sequence that hybridizes under stringent conditions to a base sequence of a gene encoding the enzyme or a base sequence complementary to the equivalent base sequence.
- the “stringent conditions” here are conditions under which so-called specific hybrids are formed and non-specific hybrids are not formed. Such stringent conditions are known to those skilled in the art, such as Molecular Cloning (Third Edition, Cold Spring Harbor Laboratory Press, New York) and Current protocols in molecular biology (edited by Frederick M. Ausubel et al., 1987) Can be set with reference to.
- hybridization solution 50% formamide, 10 ⁇ SSC (0.15M NaCl, 15 mM sodium citrate, pH 7.0), 5 ⁇ Denhardt solution, 1% SDS, 10% dextran sulfate, 10 ⁇ g / ml denaturation
- 5 ° C to about 50 ° C using salmon sperm DNA, 50 mM phosphate buffer (pH 7.5), followed by washing at about 65 ° C to about 70 ° C using 0.1 x SSC and 0.1% SDS Can be mentioned.
- More preferable stringent conditions include, for example, 50% formamide, 5 ⁇ SSC (0.15M NaCl, 15 mM sodium citrate, pH 7.0), 1 ⁇ Denhardt solution, 1% SDS, 10% dextran sulfate, 10 ⁇ g / ml as a hybridization solution. Of denatured salmon sperm DNA, 50 mM phosphate buffer (pH 7.5)).
- nucleic acid having a base sequence of a gene encoding the present enzyme or a part of a base sequence complementary thereto.
- a nucleic acid fragment can be used for detecting, identifying, and / or amplifying a nucleic acid having a base sequence of a gene encoding this enzyme.
- the nucleic acid fragment is, for example, a nucleotide portion continuous in the base sequence of the gene encoding the present enzyme (eg, about 10 to about 100 bases in length, preferably about 20 to about 100 bases in length, more preferably about 30 to about 100 bases in length). It is designed to include at least a portion that hybridizes to the.
- a nucleic acid fragment can be labeled.
- fluorescent substances, enzymes, and radioisotopes can be used.
- Still another aspect of the present invention relates to a recombinant DNA containing the gene of the present invention (gene encoding the enzyme).
- the recombinant DNA of the present invention is provided, for example, in the form of a vector.
- vector refers to a nucleic acid molecule capable of transporting a nucleic acid inserted therein into a target such as a cell.
- An appropriate vector is selected according to the purpose of use (cloning, protein expression) and in consideration of the type of host cell.
- Examples of vectors that use insect cells as hosts include pAc and pVL, and examples of vectors that use mammalian cells as hosts include pCDM8 and pMT2PC.
- the vector of the present invention is preferably an expression vector.
- “Expression vector” refers to a vector capable of introducing a nucleic acid inserted therein into a target cell (host cell) and allowing expression in the cell.
- Expression vectors usually contain a promoter sequence necessary for the expression of the inserted nucleic acid, an enhancer sequence that promotes expression, and the like.
- An expression vector containing a selectable marker can also be used. When such an expression vector is used, the presence / absence (and extent) of introduction of the expression vector can be confirmed using a selection marker.
- Insertion of the nucleic acid of the present invention into a vector, insertion of a selectable marker gene (if necessary), insertion of a promoter (if necessary), etc. are performed using standard recombinant DNA techniques (for example, Molecular Cloning, Third Edition, 1.84, Cold Spring Harbor Laboratory Press and New York, which can be referred to, are known methods using restriction enzymes and DNA ligases).
- bacteria Esscherichia coli, Bacillus subtilis, etc.
- yeasts Sacharomyces cerevisiae, etc.
- Pichia genus Pichia pastoris, etc.
- microorganisms such as filamentous fungi (such as Aspergillus eoryzae) and actinomycetes (such as genus Streptomyces), but in host cells capable of replicating recombinant DNA and expressing the gene of this enzyme.
- E. coli include E. coli BL21 (DE3) when using a T7 promoter, and E. coli JM109 and DH5 ⁇ otherwise.
- yeast include budding yeast SHY2, budding yeast AH22, or budding yeast INVSc1 (Invitrogen), and yeast Pichia pastris GS115 (Thermo Fisher Science).
- Still another aspect of the present invention relates to a microorganism (that is, a transformant) having the recombinant DNA of the present invention.
- the microorganism of the present invention can be obtained by transfection or transformation using the vector of the present invention.
- calcium chloride method Frnal of Molecular Biology (J. Mol. Biol.), Volume 53, pp. 159 (1970)
- Hanahan Method Journal of Molecular Biology, Volume 166, 557) (1983
- SEM Gene, 96, 23 (1990)
- Chung et al. Proceedings of the National Academy of Sciences of the USA, 86 Vol., P.
- microorganism of the present invention can be used for producing this enzyme. it can.
- a further aspect of the invention provides a method for producing the enzyme.
- a step of culturing a microorganism that produces the enzyme (step (1)) and a step of recovering lipase from the culture solution and / or cells after the culture (step (2)).
- the microorganism producing this enzyme is Candida parargosa, and preferably Candida parargosa NBRC 0966 strain or a mutant thereof. Mutant strains can be obtained by irradiation with ultraviolet rays, X-rays, ⁇ -rays, treatment with nitrous acid, hydroxylamine, N-methyl-N′-nitro-N-nitrosoguanidine, and the like.
- the mutant strain is not limited as long as the enzyme is produced. Examples of mutant strains include strains with improved productivity of the present enzyme, strains with reduced productivity of contaminants, strains that are easier to culture, strains that are easier to recover from the culture medium, and the like.
- Culture conditions and culture methods are not particularly limited as long as this enzyme is produced. That is, on the condition that the present enzyme is produced, a method and culture conditions suitable for culturing the microorganism to be used can be appropriately set.
- the culture method may be either liquid culture or solid culture, but preferably liquid culture is used. Taking liquid culture as an example, the culture conditions will be described.
- the medium is not particularly limited as long as the microorganism to be used can grow.
- carbon sources such as glucose, sucrose, gentiobiose, soluble starch, glycerin, dextrin, molasses, organic acids, ammonium sulfate, ammonium carbonate, ammonium phosphate, ammonium acetate, or peptone, yeast extract, corn steep liquor, casein
- Nitrogen sources such as hydrolysates, bran and meat extracts, and further added with inorganic salts such as potassium salts, magnesium salts, sodium salts, phosphates, manganese salts, iron salts and zinc salts can be used.
- vitamins, amino acids and the like may be added to the medium.
- the pH of the medium is adjusted to, for example, about 3 to 8, preferably about 4 to 7, and the culture temperature is usually about 20 to 40 ° C., preferably about 25 to 35 ° C. for 1 to 20 days, preferably 3 to Incubate for about 10 days under aerobic conditions.
- the culture method for example, a shaking culture method or an aerobic deep culture method using a jar fermenter can be used.
- the target enzyme is recovered from the culture broth or cells (step (2)).
- the culture supernatant is filtered, centrifuged, etc. to remove insolubles, concentrated by ultrafiltration membrane, salting out such as ammonium sulfate precipitation, dialysis, ion exchange resin, etc.
- the present enzyme can be obtained by performing separation and purification by appropriately combining various types of chromatography.
- the microbial cells are crushed by pressure treatment, ultrasonic treatment, etc., and then separated and purified in the same manner as described above to obtain the enzyme.
- recovering a microbial cell from a culture solution previously by filtration, a centrifugation process, etc. you may perform the said series of processes (crushing, isolation
- the degree of purification of the enzyme is not particularly limited.
- the enzyme can be purified to a specific activity of 0.5 to 20 (U / mg), preferably 5 to 20 (U / mg).
- the final form may be liquid or solid (including powder).
- the present enzyme is produced using the above transformant.
- the above-mentioned transformant is cultured under the condition that a protein encoded by the gene introduced therein is produced (step (i)).
- Culture conditions for transformants are known for various vector host systems, and those skilled in the art can easily set appropriate culture conditions.
- the produced protein ie, the present enzyme
- recovery and subsequent purification may be performed in the same manner as in the above embodiment.
- the purified enzyme obtained as described above by pulverizing it by, for example, freeze drying, vacuum drying or spray drying.
- the purified enzyme may be dissolved in advance in an acetate buffer, phosphate buffer, triethanolamine buffer, Tris-HCl buffer or GOOD buffer.
- acetate buffer, phosphate buffer, and triethanolamine buffer can be used.
- PIPES, MES, or MOPS is mentioned as a GOOD buffer here.
- cell-free synthesis system (cell-free transcription system, cell-free transcription / translation system) refers to a ribosome derived from a live cell (or obtained by a genetic engineering technique), not a live cell. This refers to the in vitro synthesis of mRNA and protein encoded by a template nucleic acid (DNA or mRNA) using transcription / translation factors.
- a cell extract obtained by purifying a cell disruption solution as needed is generally used.
- Cell extracts generally contain ribosomes necessary for protein synthesis, various factors such as initiation factors, and various enzymes such as tRNA.
- ribosomes necessary for protein synthesis
- various factors such as initiation factors
- various enzymes such as tRNA.
- other substances necessary for protein synthesis such as various amino acids, energy sources such as ATP and GTP, and creatine phosphate are added to the cell extract.
- a ribosome, various factors, and / or various enzymes prepared separately may be supplemented as necessary during protein synthesis.
- cell-free transcription / translation system is used interchangeably with a cell-free protein synthesis system, in-vitro translation system or in-vitro transcription / translation system.
- RNA is used as a template to synthesize proteins.
- total RNA, mRNA, in vitro transcript and the like are used.
- the other in vitro transcription / translation system uses DNA as a template.
- the template DNA should contain a ribosome binding region and preferably contain an appropriate terminator sequence.
- conditions to which factors necessary for each reaction are added are set so that the transcription reaction and the translation reaction proceed continuously.
- this enzyme (Random transesterification of fats and oils)
- the further situation of this invention is related with the use of this enzyme, and provides the random transesterification method of the fats and oils using this enzyme.
- this enzyme is used as a catalyst.
- a step of causing the enzyme to act on fats and oils is performed, and by this step, random transesterification of fats and oils, that is, reconstituting fatty acids constituting triacylglycerol (abbreviated as TG or TAG) in the fats and oils. (Rearrange).
- soybean oil, rapeseed oil, rice oil, corn oil, sunflower oil, cottonseed oil, peanut oil, safflower oil, palm oil, palm soft oil, palm fractionated oil, palm examples include vegetable oils such as kernel oil, coconut oil and cacao butter, animal oils such as fish oil, lard, beef tallow and milk fat, and fractionated oils thereof, hardened oil, synthetic oils such as trilaurin, triolein and tripalmitin.
- the random transesterification method of the present invention can be used for transesterification between fats and oils and fatty acids or fatty acid esters, as well as transesterification between fats and oils.
- fatty acids examples include stearic acid, palmitic acid, lauric acid, arachidic acid, behenic acid, oleic acid, linoleic acid, and examples of fatty acid esters are ethyl stearate, ethyl palmitate, ethyl oleate, ethyl linoleate.
- the present enzyme is added to fats and oils (an enzyme agent containing the present enzyme may be added), for example, at 30 to 100 ° C., preferably at 35 to 80 ° C.
- the reaction is performed for a predetermined time (for example, 5 to 48 hours). In order to promote the reaction, stirring may be performed during the reaction.
- the immobilized enzyme may be used as an enzyme to be subjected to the reaction.
- a batch type stirred tank type reactor a flow type stirred tank type reactor, a packed bed type reactor, a fluidized bed type reactor or the like can be used.
- the random transesterification method of the present invention is useful for improving and improving the physical properties of fats and oils or processed oils (for example, shortening, margarine). For example, improvement of spreadability, improvement of emulsion stability, optimization of solid fat content (SFC), improvement of solidification, selective concentration of specific fatty acids, production of low trans acid oils or processed products of low trans acid oils
- the random transesterification method of the present invention can be applied.
- the fats and oils obtained by applying the random transesterification method of the present invention or the processed fats and oils containing the fats and oils have improved physical properties as compared with those before treatment, and have high industrial utility value.
- random transesterified fats and oils can be produced according to the random transesterification method of the present invention. That is, this invention also provides the manufacturing method of random transesterified fats and oils.
- an acceptor substrate oil (triglyceride), glycerin fatty acid ester (diglyceride, monoglyceride), glycerin) and a donor substrate (fatty acid, ester compound (fatty acid ester, etc.) )
- a step of allowing the enzyme of the present invention to act that is, an enzyme reaction in the presence of the acceptor substrate and the donor substrate).
- the oils, fatty acids, and fatty acid esters used for the acceptor substrate and donor substrate can be those described above.
- the enzyme reaction conditions for example, 30 to 100 ° C., preferably 35 to 80 ° C., reaction for a predetermined time (for example, 5 to 48 hours)) can be employed.
- lipase activity (hydrolysis activity) was measured using lipase kit S (manufactured by DS Pharma) according to the manual attached to the kit. However, the attached buffer adjusted to pH 7 was used as the buffer, and acetone was used as the reaction stop solution. The lipase activity was calculated from the following formula.
- U / mL (A412 sample-A412 blank) x 1 / 0.05 x n (However, A412 sample is the absorbance at 412 nm of the sample, A412 blank is the absorbance at 412 nm of the blank, 0.05 is the amount of sample added (mL), and n is the dilution factor)
- lipase kit S coloring stock solution 0.05 mL of lipase kit S coloring stock solution and 0.05 mL of lipase kit S substrate solution were added to 0.45 mL of 0.5 M PIPES solution (pH 7), and the mixture was heated at 30 ° C. for 5 minutes.
- 0.025 mL of the enzyme solution was added and reacted for exactly 15 minutes, and then 1 mL of ethanol was added to stop the reaction. The supernatant was collected by centrifugation and the absorbance (412 nm) was measured. The lipase activity was calculated using the above formula.
- ⁇ Random transesterification activity measurement method> The enzyme solution was lyophilized, 1 mL of cocoa butter (manufactured by Daito Cacao) and 2 ⁇ L of ultrapure water were added per 1 U of enzyme (lipase activity), and the mixture was reacted at 60 ° C. with stirring. The reaction solution was sampled at each measurement time, and 10 ⁇ L was dissolved in 1 mL of hexane to obtain a sample for gas chromatography. Gas chromatography analysis (column: DB-1HT (J & W, 5 m ⁇ 0.25 mm, df 0.1 ⁇ m), temperature condition: 120 ° C., hold for 4 minutes, then heat up to 150 ° C.
- DB-1HT J & W, 5 m ⁇ 0.25 mm, df 0.1 ⁇ m
- composition ratio of tripalmitin (C48) (PPP) in the triglyceride molecular species is calculated using the vessel: FID, carrier gas: helium, and the C48 production ratio is increased, that is, “(in the triglyceride fraction of the reaction fat and oil Random transesterification ability of each enzyme was evaluated using as an index the composition ratio of PPP ⁇ (composition ratio of PPP in the triglyceride fraction of the substrate fat / oil) ”( ⁇ PPP (%)).
- the culture solution obtained by liquid culture of the strain selected in the primary screening was pulverized by vacuum drying at 60 ° C., and 1 mL of cocoa butter and 2 ⁇ l of water were added, followed by reaction for 8 days.
- Strains (Table 1) in which the production of tripalmitin as an indicator of random transesterification was confirmed by gas chromatography (GC) were subjected to the next screening.
- the main culture medium was put in a 30 L jar fermenter and steam-sterilized, and then the preculture solution was added, followed by culturing at 27 ° C., agitation number of 250 rpm, and aeration rate of 0.5 vvm for 4 days to obtain a culture solution.
- the obtained culture solution was centrifuged, and the culture supernatant was collected.
- the culture supernatant was subjected to diatomaceous earth filtration to obtain a clarified liquid.
- the clear solution was concentrated and desalted by ultrafiltration, and the obtained desalted solution (crude enzyme solution) was freeze-dried to obtain a crude enzyme powder. Part of the crude enzyme solution was used for enzyme purification.
- the fraction with active activity (active main peak fraction) was treated with Endo-Hf (manufactured by New England Biolabs) (removal of N-type sugar chains), and the molecular weight before and after treatment was compared by SDS-PAGE. .
- FIG. 6A The results of SDS-PAGE of the purified fraction are shown in FIG. 6A.
- FIG. 6B shows the result of Endo-Hf treatment of the active main peak fraction.
- the molecular weight of the target enzyme (lipase) after Endo-Hf treatment (after removal of the N-type sugar chain) was about 36 kDa.
- the N-terminal amino acid sequence was VTDEPLENVPGILSHPTI (SEQ ID NO: 1).
- a database search was performed based on this N-terminal sequence, but no homologous protein was found.
- Random transesterification activity was measured using a purified fraction (fractions 48 to 52 were collected and concentrated and desalted). As a result, the production of tripalmitin (PPP) was confirmed in the purified fraction (FIG. 7), indicating that the target enzyme was successfully purified.
- PPP tripalmitin
- CDNA was synthesized using SuperScript TM III First-Strand Synthesis System (manufactured by Thermo Fisher Science) according to the attached protocol.
- a primer homologous to the upstream of the structural gene (RELFUP: 5'-CACATCTCAATAGCATCA-3 ': SEQ ID NO: 6) and a primer homologous to the downstream of the structural gene (RELEDOWN: 5'- Using AGCTGGGTATGTTCAGAAGTTAA-3 ′: SEQ ID NO: 7)
- PCR was performed using PrimeSTAR (registered trademark) Max DNA Polymerase (manufactured by Takara Bio Inc.) according to the attached protocol.
- the amplification product of about 1000 bp confirmed to be amplified was cloned using Mighty TA-cloning Kit (manufactured by Takara Bio Inc.) to confirm the sequence (SEQ ID NO: 5).
- cDNA sequence (SEQ ID NO: 5) from the start codon to the end codon was amplified by PCR and cloned into the snaBI site of pPick3.5k (manufactured by Thermo Fisher Science) in accordance with a conventional method to prepare an expression vector pPick3.5k-REL.
- pPick3.5k-REL was cleaved with restriction enzyme SalI, and linear DNA was recovered by ethanol precipitation.
- Pichia pastris GS115 manufactured by Thermo Fisher Science was transformed by electroporation according to a conventional method to obtain a transformant.
- Transformants were transformed into BMGY medium (2% bactopeptone, 1% yeast extract, 1% glycerin, 0.67% yeast nitrogen base (YNB (including ammonium sulfate, no amino acids)), 100 mM potassium phosphate buffer (pH 6). 0.0)% 0.00004% D-biotin) at 30 ° C.
- BMMY medium 2% bactopeptone, 1% yeast extract, 0.5% methanol, 0.67% yeast nitrogen base
- the suspension was suspended in YNB (containing ammonium sulfate, no amino acid)), 100 mM potassium phosphate buffer (pH 6.0), 0.00004% D-biotin), and cultured at 30 ° C. for 3 days while adding methanol as appropriate.
- the supernatant was collected by centrifugation to obtain a crude enzyme solution.
- the lipase activity of the obtained crude enzyme solution was confirmed according to the above method.
- the 5 'terminal 63 bases of the sequence of SEQ ID NO: 5 is a signal sequence, and the sequence excluding the signal sequence (SEQ ID NO: 4) encodes the amino acid sequence (SEQ ID NO: 2) of the mature enzyme (not including the signal peptide) To do.
- the random transesterification lipase of the present invention has high heat resistance and is suitable for use in food applications.
- the random transesterification lipase of the present invention is used for modifying edible fats and oils such as margarine and shortening.
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Abstract
Description
[1]下記の酵素化学的性質を有するリパーゼ、
(1)作用:ランダムエステル交換反応を触媒する、
(2)分子量:N型糖鎖を含まない場合の分子量が約36 kDa(SDS-PAGEによる)、
(3)油脂中での温度安定性:60℃以下で安定(トリカプリリンとステアリン酸メチルを基質とし、カプリリン酸メチル生成量を指標とした評価による)、
(4)油脂中での反応性:40~80℃で反応させた場合に、80℃で最も高い反応性を示す(カカオバターを基質とし、トリパルミチン生成量を指標とした評価による)。
[2]下記の酵素化学的性質を更に有する、[1]に記載のリパーゼ、
(5)pH安定性:pH3~7の範囲で安定(30℃、1時間)、
(6)至適pH:6。
[3]N末端アミノ酸配列がVTDEPLENVPGILSHPTI(配列番号1)である、[1]又は[2]に記載のリパーゼ。
[4]カンジダ・パラルゴッサ由来である、[1]~[3]のいずれか一項に記載のリパーゼ。
[5]カンジダ・パラルゴッサがNBRC 0966株又はその変異株である、[4]に記載のリパーゼ。
[6]配列番号2に示すアミノ酸配列、又は該アミノ酸配列と等価なアミノ酸配列を有するリパーゼ。
[7]等価なアミノ酸配列が、配列番号2に示すアミノ酸配列と70%以上同一のアミノ酸配列である、[6]に記載のリパーゼ。
[8][1]~[7]のいずれか一項に記載のリパーゼを含む酵素剤。
[9][1]~[7]のいずれか一項に記載のリパーゼを油脂に作用させるステップを含む、油脂のランダムエステル交換法。
[10]以下のステップ(1)及び(2)を含む、ランダムエステル交換用リパーゼの製造法:
(1)カンジダ・パラルゴッサを培養するステップ;
(2)培養後の培養液及び/又は菌体よりリパーゼを回収するステップ。
[11]カンジダ・パラルゴッサがNBRC 0966株である、[10]に記載の製造法。
[12][1]~[7]のいずれか一項に記載のリパーゼを油脂に作用させるステップを含む、ランダムエステル交換油脂の製造方法。
[13]以下の(a)~(c)からなる群より選択されるいずれかのDNAからなるリパーゼ遺伝子:
(a)配列番号2のアミノ酸配列、又は該アミノ酸配列と等価なアミノ酸配列をコードするDNA;
(b)配列番号4又は5の塩基配列からなるDNA;
(c)配列番号4又は5の塩基配列と等価な塩基配列を有し、且つランダムエステル交換活性を有するタンパク質をコードするDNA。
[14][13]に記載のリパーゼ遺伝子を含む組換えDNA。
[15][14]に記載の組換えDNAを保有する微生物。
[16]以下のステップ(i)及び(ii)を含む、リパーゼの製造法:
(i)[15]に記載の微生物を、前記遺伝子がコードするタンパク質が産生される条件下で培養するステップ;
(ii)産生された前記タンパク質を回収するステップ。
本明細書において用語「単離された」は「精製された」と交換可能に使用される。用語「単離された」は、天然の状態、即ち、自然界において存在している状態のものと区別するために使用される。単離するという人為的操作によって、天然の状態とは異なる状態である、「単離された状態」となる。単離されたものは、天然物自体と明確且つ決定的に相違する。
本発明の第1の局面は、本発明者らが取得・同定に成功し、その有用性を見出した新規リパーゼに関する。本発明のリパーゼ(以下、「本酵素」ともいう)は、以下の酵素化学的性質を備えることを特徴とする。
(1)作用
本酵素はリパーゼであり、ランダムエステル交換反応を触媒する。ランダムエステル交換活性は、カカオバター(カカオ脂)を基質とした方法(後述の「ランダムエステル交換活性測定法」)で評価することができる。カカオバターはオレイン酸、パルミチン酸、ステアリン酸等を構成脂肪酸として含み、主に2位にオレイン酸が結合したトリグリセリドを主成分とする。その為、パルミチン酸が1位、2位、3位の全てに結合しているトルパルミチン(PPP)はランダムエステル交換反応によってのみ生じる(1位又は3位のパルミチン酸を2位のオレイン酸と交換する必要があり、1位、3位特異的なリパーゼで反応をさせた場合は、2位にパルミチン酸が挿入されたトリグリセリドは生じない)。従って、トリパルミチン生成量を指標としてランダムエステル交換活性を評価することができる。後述のランダムエステル交換活性測定法にて評価した場合に、反応によってトリパルミチン(C48)の生成比が上昇していればランダムエステル交換反応を触媒すると言える。上昇の程度は特に限定されないが、好ましくはΔPPP(%)が0.01以上、より好ましくはΔPPP(%)が0.03以上、更に好ましくはΔPPP(%)が0.05以上であることが望ましい。
本酵素は天然型(カンジダ・パラルゴッサが産生する場合)では糖鎖を含み(即ち、糖タンパク質である)、N型糖鎖除去後の分子量、即ち、N型糖鎖を含まない場合の本酵素の分子量は約36 kDa(SDS-PAGEで測定した分子量)である。
油脂中での温度安定性は、トリカプリリンとステアリン酸メチルを基質とし、カプリリン酸メチル生成量を指標とした方法(詳細は後述する)によって評価することができる。本発明の酵素では、トリカプリリン中、1時間処理した場合、60℃以下であれば90%以上の活性を維持する。このように優れた温度安定性を示す本酵素は、比較的高温での処理が必要な食品用途(例えば融点の高い油脂の加工など)に適する。
油脂中での反応性は、カカオバターを基質とし、トリパルミチン生成量を指標とした方法(詳細は後述する)によって評価することができる。本酵素の油脂中において40~80℃で反応させた場合に、80℃で最も高い反応性を示す。このように高温での反応性が高いことは、比較的高温での処理が必要な食品用途(例えば融点の高い油脂の加工など)に適する。
(5)pH安定性
本酵素はpH3~7で安定した活性を示す。例えば、処理に供する酵素溶液のpHが3~7の範囲内にあれば、30℃、1時間の処理後、最大活性の80%以上の活性を示す。尚、pH安定性は、例えば、pH2~3のpH域ではグリシン-塩酸緩衝液中、pH3~6のpH域ではクエン酸緩衝液中、pH6~8のpH域ではリン酸緩衝液中、pH8~9のpH域ではTris-塩酸緩衝液中、pH9~11のpH域では炭酸ナトリウム緩衝液中で測定した結果を基に判断される。
本酵素の至適pHは6である。至適pHは、例えば、ブリトンロビンソン緩衝液(pH2~9)中で測定した結果を基に判断される。
本酵素は例えば酵素剤の形態で提供される。酵素剤は、有効成分(本酵素)の他、賦形剤、緩衝剤、懸濁剤、安定剤、保存剤、防腐剤、生理食塩水などを含有していてもよい。有効成分である本酵素の精製度は特に問わない。即ち、粗酵素であっても精製酵素であってもよい。賦形剤としては乳糖、ソルビトール、D-マンニトール、マルトデキストリン、白糖等を用いることができる。緩衝剤としてはリン酸塩、クエン酸塩、酢酸塩等を用いることができる。安定剤としてはプロピレングリコール、アスコルビン酸等を用いることができる。保存剤としてはフェノール、塩化ベンザルコニウム、ベンジルアルコール、クロロブタノール、メチルパラベン等を用いることができる。防腐剤としては塩化ベンザルコニウム、パラオキシ安息香酸、クロロブタノール等と用いることができる。
本発明の第2の局面は本酵素に関連する核酸を提供する。即ち、本酵素をコードする遺伝子、本酵素をコードする核酸を同定するためのプローブとして用いることができる核酸、本酵素をコードする核酸を増幅又は突然変異等させるためのプライマーとして用いることができる核酸が提供される。
本発明の更なる局面は本酵素の製造法を提供する。本発明の製造法の第1態様では、本酵素を産生する微生物を培養するステップ(ステップ(1))と培養後の培養液及び/又は菌体よりリパーゼを回収するステップ(ステップ(2))を行う。本酵素を産生する微生物はカンジダ・パラルゴッサであり、好ましくは、カンジダ・パラルゴッサNBRC 0966株又はその変異株である。変異株は、紫外線、X線、γ線などの照射、亜硝酸、ヒドロキルアミン、N-メチル-N'-ニトロ-N-ニトロソグアニジンなどによる処理等によって得ることができる。変異株は、本酵素を産生する限り限定されない。変異株として、本酵素の生産性が向上した株、夾雑物の生産性が低減した株、培養が容易になった株、培養液からの回収が容易になった株などが挙げられる。
本発明の更なる局面は本酵素の用途に関し、本酵素を用いた油脂のランダムエステル交換法を提供する。本発明のランダムエステル交換法では本酵素を触媒として用いる。換言すれば、本発明では本酵素を油脂に作用させるステップを行い、当該ステップによって油脂のランダムエステル交換、即ち、油脂中のトリアシルグリセロール(TG又はTAGと略称される)の構成脂肪酸を再編成(再配列)させる。
特に記載がない限り、リパーゼ活性(加水分解活性)の測定はリパーゼキットS(DSファーマ製)を使用し、キット添付のマニュアルに従い行った。但し、緩衝液にはpH7に調整した付属緩衝液を使用し、反応停止液にはアセトンを使用した。以下計算式によってリパーゼ活性を算出した。
U/mL=(A412 sample-A412 blank)×1/0.05 × n
(但し、A412 sampleはサンプルの412nmの吸光度、A412 blankはブランクの412nmの吸光度、0.05はサンプル添加量(mL)、nは希釈倍率)
以下の緩衝液、即ち、1M グリシン-塩酸緩衝液(pH2,3)、1M クエン酸緩衝液(pH3,4,5,6)、1M リン酸緩衝液(pH6,7,8)、1M Tris-塩酸緩衝液(pH8,9)、1M 炭酸ナトリウム緩衝液(pH9,10,11)を使用した。酵素溶液を等量の各緩衝液と混合し、30℃にて1時間処理した。処理後のサンプルを用い、以下の方法でリパーゼ活性を測定した。まず、0.5M PIPES溶液(pH7) 0.45mLにリパーゼキットS発色原液0.05mLとリパーゼキットS基質液0.05mLを添加し、30℃で5分間加温した。次に、酵素溶液を0.025mL添加し、正確に15分間反応させた後、1mLのエタノールを添加して反応を停止させた。遠心処理して上清を回収し、吸光度(412nm)を測定した。上記の計算式を用い、リパーゼ活性を算出した。
緩衝液として20mMブリトンロビンソン緩衝液(pH 2,3,4,5,6,7,8,9)を使用した。各緩衝液0.45mLにリパーゼキットS発色原液0.05mLとリパーゼキットS基質液0.05mLを添加し、30℃で5分間加温した。酵素溶液を0.025mL添加し、正確に15分間反応させた後、1mLのリパーゼキットS反応停止液を添加して反応を停止させた。1mLの1M Tris-HCl(pH9)を添加後、直ぐに吸光度(412nm)を測定した。上記の計算式を用い、リパーゼ活性を算出した。
酵素溶液を凍結乾燥させ、酵素1U(リパーゼ活性)あたり1mLのカカオバター(大東カカオ製)と2μLの超純水を添加し、60℃で撹拌しながら反応させた。各測定時間で反応液をサンプリングし、10μLを1mLのヘキサンに溶解させ、ガスクロマトグラフィー用サンプルとした。ガスクロマトグラフィー分析(カラム:DB-1HT(J&W社, 5 m×0.25 mm, df 0.1μm)、温度条件:120℃、4分間保持後、20℃/分の速度で150℃まで昇温、さらに30℃/分の速度で315℃まで昇温後3分間保持、その後1.5℃/分の速度で325℃まで昇温、さらに30℃/分の速度で370℃まで昇温後2分間保持、検出器:FID、キャリアーガス:ヘリウム)により、トリグリセリド分子種中のトリパルミチン(C48)(PPP)の組成比を算出し、C48の生成比の上昇、即ち、「(反応油脂のトリグリセリド画分中のPPPの組成比)-(基質油脂のトリグリセリド画分中のPPPの組成比)」(ΔPPP(%))を指標として、各酵素のランダムエステル交換能を評価した。
(1)温度安定性の評価
凍結乾燥した1U相当の酵素粉末に、トリカプリリン(和光純薬工業(株)製)0.5mLを添加し、よく懸濁した。各温度で1時間熱処理を実施した。各液を60℃で10分間プレインキュベーションした後、60℃で予熱しておいたステアリン酸メチル(和光純薬工業(株)製)0.5mLを添加しよく懸濁し、60℃で酵素反応を2時間行った。反応後の溶液30μLを1mLのヘキサンに溶解させガスクロマトグラフィーのサンプルとした。
5U相当の酵素粉末(凍結乾燥体)をカカオバターに懸濁し、カカオバター1mLあたり2μLの精製水を添加し、反応を開始した。反応開始8時間後のトリパルミチン生成量を反応温度間で比較した。
ランダムエステル交換活性を示す菌を見出すべく、細菌、酵母、糸状菌、放線菌を含む約1500株をスクリーニングに供した。1次スクリーニングでは、大豆油0.5%を含む各プレートにて菌を生育させてハローを形成させ、その後55℃でさらにインキュベートし、ハローが拡大する株を耐熱性リパーゼ生産菌として選抜した。
500mL坂口フラスコに前培養培地100mLを入れて蒸気殺菌後カンジダ・パラルゴッサ(Candida pararugosa)NBRC 0966株を1白金耳接種し、27℃で4日間培養し、前培養液を得た。
<前培養培地>
Yeast extract. (ベクトン・ディッキンソン株式会社製) 0.3%
Malto extract. (ベクトン・ディッキンソン株式会社製) 0.3%
Bacto Peptone (ベクトン・ディッキンソン株式会社製) 0.5%
含水結晶ブドウ糖 1.0%
大豆サラダ油 0.5%
pH 6.2
<本培養培地>
Yeast extract. (ベクトン・ディッキンソン株式会社製) 0.9%
Malto extract. (ベクトン・ディッキンソン株式会社製) 0.9%
Peptone (ベクトン・ディッキンソン株式会社製) 1.5%
含水結晶ブドウ糖(サンエイ糖化製) 3.0%
大豆サラダ油(日清オイリオ) 1.5%
pH 6.2
(1)pH安定性と至適pH
粗酵素粉末を水に溶解し、酵素溶液とした。酵素溶液を用い、上記の測定法でpH安定性と至適pHを測定した。測定結果を図1(pH安定性)と図2(至適pH)に示す。pH3~7で高い活性維持(30℃で1時間処理後80%以上残存)し、至適pHは6であった。
粗酵素粉末を用い、上記の評価法で油脂中での温度安定性と反応性を評価した。結果を図3(温度安定性)と図4(反応性)に示す。60℃まで安定であり(トリカプリリン中、1時間処理した場合、60℃以下であれば90%以上の活性を維持)、温度安定性に優れていた。また、油脂中において40~80℃の範囲では80℃で最も高い反応性を示した。
粗酵素液を疎水クロマトグラフィー(Butyl-HP(GEヘルスケア製))に供した。カラムは20mMリン酸緩衝液 pH7.0で平衡化し、硫安(0.5→0M) 30CVのリニアグラジエントで溶出した。リパーゼ活性(加水分解活性)を指標に分画した。精製チャートを図5に示す。リパーゼ活性を含む複数の画分を確認できたため、これらの画分をSDS-PAGEに供した。一方、活性がピークとなる画分(活性メインピーク画分)についてはEndo-Hf(New England Biolabs製)で処理し(N型糖鎖の除去)、処理前後の分子量をSDS-PAGEで比較した。
精製画分(画分48~52を回収し、濃縮脱塩したもの)を使用し、ランダムエステル交換活性を測定した。その結果、精製画分においてもトリパルミチン(PPP)の生成が確認でき(図7)、目的の酵素の精製に成功していることが示された。
C. pararugosa NBRC 0966株を、0.5% 大豆サラダ油を添加したYM培地(Yeast extract. (Bacto) 0.9%、Malto extract. (Bacto) 0.9%、Peptone (Bacto) 1.5%、含水結晶ブドウ糖3.0%、大豆サラダ油1.5%)(pH6.2)にて1日間培養し、菌体を遠心分離で回収した。回収した菌体はTE緩衝液(pH8.0)を用いて、十分に洗浄した。獲得した菌体は、液体窒素下で、乳鉢と乳棒を用いてすり潰した。RNAiso Plus(タカラバイオ製)を使用し、すり潰した菌体から、添付のプロトコールに従ってtotal RNAを抽出した。続いて、OligotexTM -dT30<Super> mRNA Purification Kit(タカラバイオ製)を使用し、抽出したRNAから、添付のプロトコールに従ってmRNAを調製した。
Pichia発現系を利用し、得られたcDNAが目的酵素の遺伝子であることを確認した。cDNA配列(配列番号5)の開始コドンから終始コドンまでをPCRで増幅し、pPick3.5k(サーモフィッシャーサイエンス製)のsnaBIサイトに常法に従ってクローニングし、発現ベクターpPick3.5k-RELを作成した。pPick3.5k-RELを制限酵素SalIで切断し、エタノール沈殿により直鎖状DNAを回収した。回収したDNAを用い、定法に従ってPichia pastris GS115(サーモフィッシャーサイエンス製)をエレクトロポレーションで形質転換し、形質転換体を得た。形質転換体をBMGY培地(2%バクトペプトン、1%イーストエキストラクト、1%グリセリン、0.67%イーストニトロゲンベース(YNB(硫酸アンモニウムを含む、アミノ酸を含まない))、100mMリン酸カリウム緩衝液(pH6.0)、0.00004% D-ビオチン)で30℃、2日間培養し、得られた菌体をBMMY培地(2%バクトペプトン、1%イーストエキストラクト、0.5%メタノール、0.67%イーストニトロゲンベース(YNB(硫酸アンモニウムを含む、アミノ酸を含まない))、100mMリン酸カリウム緩衝液(pH6.0)、0.00004% D-ビオチン)に懸濁し、メタノールを適宜添加しながら30℃、3日間培養した。遠心分離により上清を回収し、粗酵素液を得た。得られた粗酵素液のリパーゼ活性を前記方法に従い確認した。
得られた粗酵素液を用いて、ランダムエステル交換活性を前記方法に従い確認した。その結果を図8に示す。トリパルミチン(PPP)の生成が認められ(図8)、配列番号5の配列が目的酵素(ランダムエステル交換活性を示すリパーゼ)の遺伝子(cDNA)であることが確認された。配列番号5の配列がコードする目的酵素のアミノ酸配列を配列番号3に示す。配列番号5の配列の5'末端側63塩基はシグナル配列であり、シグナル配列を除いた配列(配列番号4)が成熟体酵素(シグナルペプチドを含まない)のアミノ酸配列(配列番号2)をコードする。
Claims (16)
- 下記の酵素化学的性質を有するリパーゼ、
(1)作用:ランダムエステル交換反応を触媒する、
(2)分子量:N型糖鎖を含まない場合の分子量が約36 kDa(SDS-PAGEによる)、
(3)油脂中での温度安定性:60℃以下で安定(トリカプリリンとステアリン酸メチルを基質とし、カプリリン酸メチル生成量を指標とした評価による)、
(4)油脂中での反応性:40~80℃で反応させた場合に、80℃で最も高い反応性を示す(カカオバターを基質とし、トリパルミチン生成量を指標とした評価による)。 - 下記の酵素化学的性質を更に有する、請求項1に記載のリパーゼ、
(5)pH安定性:pH3~7の範囲で安定(30℃、1時間)、
(6)至適pH:6。 - N末端アミノ酸配列がVTDEPLENVPGILSHPTI(配列番号1)である、請求項1又は2に記載のリパーゼ。
- カンジダ・パラルゴッサ由来である、請求項1~3のいずれか一項に記載のリパーゼ。
- カンジダ・パラルゴッサがNBRC 0966株又はその変異株である、請求項4に記載のリパーゼ。
- 配列番号2に示すアミノ酸配列、又は該アミノ酸配列と等価なアミノ酸配列を有するリパーゼ。
- 等価なアミノ酸配列が、配列番号2に示すアミノ酸配列と70%以上同一のアミノ酸配列である、請求項6に記載のリパーゼ。
- 請求項1~7のいずれか一項に記載のリパーゼを含む酵素剤。
- 請求項1~7のいずれか一項に記載のリパーゼを油脂に作用させるステップを含む、油脂のランダムエステル交換法。
- 以下のステップ(1)及び(2)を含む、ランダムエステル交換用リパーゼの製造法:
(1) カンジダ・パラルゴッサを培養するステップ;
(2)培養後の培養液及び/又は菌体よりリパーゼを回収するステップ。 - カンジダ・パラルゴッサがNBRC 0966株である、請求項10に記載の製造法。
- 請求項1~7のいずれか一項に記載のリパーゼを油脂に作用させるステップを含む、ランダムエステル交換油脂の製造方法。
- 以下の(a)~(c)からなる群より選択されるいずれかのDNAからなるリパーゼ遺伝子:
(a)配列番号2のアミノ酸配列、又は該アミノ酸配列と等価なアミノ酸配列をコードするDNA;
(b)配列番号4又は5の塩基配列からなるDNA;
(c)配列番号4又は5の塩基配列と等価な塩基配列を有し、且つランダムエステル交換活性を有するタンパク質をコードするDNA。 - 請求項13に記載のリパーゼ遺伝子を含む組換えDNA。
- 請求項14に記載の組換えDNAを保有する微生物。
- 以下のステップ(i)及び(ii)を含む、リパーゼの製造法:
(i)請求項15に記載の微生物を、前記遺伝子がコードするタンパク質が産生される条件下で培養するステップ;
(ii)産生された前記タンパク質を回収するステップ。
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| WO2023116569A1 (en) | 2021-12-21 | 2023-06-29 | Novozymes A/S | Composition comprising a lipase and a booster |
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Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01501120A (ja) * | 1986-10-17 | 1989-04-20 | ノボ ノルディスク アクティーゼルスカブ | 位置非特異性リパーゼ |
| JPH0292281A (ja) * | 1988-09-28 | 1990-04-03 | Showa Denko Kk | 新規リパーゼ及びその製造方法 |
| JPH0866186A (ja) * | 1994-08-30 | 1996-03-12 | D H Ee Kodo Seisei Chushutsu Gijutsu Kenkyu Kumiai | 新規リパーゼおよびその製造法 |
| JP2005185290A (ja) * | 2005-02-28 | 2005-07-14 | Academia Sinica | 組換カンジダルゴサリパーゼ |
| WO2006059592A1 (ja) | 2004-11-30 | 2006-06-08 | The Nisshin Oillio Group, Ltd. | トランス酸含量を低減した油脂組成物の製造法および該油脂組成物を含有する加工油脂製品 |
| JP3791943B2 (ja) | 1995-06-07 | 2006-06-28 | 旭電化工業株式会社 | エステル交換油脂の製造方法 |
| JP2008194011A (ja) | 2007-02-15 | 2008-08-28 | J-Oil Mills Inc | 高液状性パーム油の製造方法および高液状性パーム油 |
| WO2012077614A1 (ja) | 2010-12-06 | 2012-06-14 | 天野エンザイム株式会社 | 油脂のランダムエステル交換法及びランダムエステル交換用リパーゼ |
| JP2018022487A (ja) | 2016-08-03 | 2018-02-08 | 三星電子株式会社Samsung Electronics Co.,Ltd. | メモリモジュール及びその動作方法 |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7834190B2 (en) * | 2006-05-26 | 2010-11-16 | Kaneka Corporation | Process for production of optically active-3-amino-2-hydroxypropionic cyclopropylamide derivatives and salts thereof |
| CN101589142B (zh) * | 2007-01-30 | 2012-06-06 | 三菱化学食品株式会社 | 甘油糖脂脂肪酶 |
-
2018
- 2018-12-27 WO PCT/JP2018/048378 patent/WO2019155790A1/ja not_active Ceased
- 2018-12-27 EP EP18904906.7A patent/EP3750991A4/en active Pending
- 2018-12-27 CN CN201880088742.0A patent/CN111684065B/zh active Active
- 2018-12-27 US US16/968,261 patent/US11549130B2/en active Active
- 2018-12-27 JP JP2019570331A patent/JPWO2019155790A1/ja active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01501120A (ja) * | 1986-10-17 | 1989-04-20 | ノボ ノルディスク アクティーゼルスカブ | 位置非特異性リパーゼ |
| JPH0292281A (ja) * | 1988-09-28 | 1990-04-03 | Showa Denko Kk | 新規リパーゼ及びその製造方法 |
| JPH0866186A (ja) * | 1994-08-30 | 1996-03-12 | D H Ee Kodo Seisei Chushutsu Gijutsu Kenkyu Kumiai | 新規リパーゼおよびその製造法 |
| JP3791943B2 (ja) | 1995-06-07 | 2006-06-28 | 旭電化工業株式会社 | エステル交換油脂の製造方法 |
| WO2006059592A1 (ja) | 2004-11-30 | 2006-06-08 | The Nisshin Oillio Group, Ltd. | トランス酸含量を低減した油脂組成物の製造法および該油脂組成物を含有する加工油脂製品 |
| JP2005185290A (ja) * | 2005-02-28 | 2005-07-14 | Academia Sinica | 組換カンジダルゴサリパーゼ |
| JP2008194011A (ja) | 2007-02-15 | 2008-08-28 | J-Oil Mills Inc | 高液状性パーム油の製造方法および高液状性パーム油 |
| WO2012077614A1 (ja) | 2010-12-06 | 2012-06-14 | 天野エンザイム株式会社 | 油脂のランダムエステル交換法及びランダムエステル交換用リパーゼ |
| JP2018022487A (ja) | 2016-08-03 | 2018-02-08 | 三星電子株式会社Samsung Electronics Co.,Ltd. | メモリモジュール及びその動作方法 |
Non-Patent Citations (17)
| Title |
|---|
| "Current protocols in molecular biology", 1987, COLD SPRING HARBOR LABORATORY PRESS |
| ALTSCHUL ET AL., AMINO ACIDS RESEARCH, vol. 25, no. 17, 1997, pages 3389 - 3402 |
| ALTSCHUL ET AL., J. MOL. BIOL., vol. 215, 1990, pages 403 - 10 |
| AROUS FATMA ET AL.: "Newly isolated yeasts from Tunisian microhabitats: Lipid accumulation and fatty acid composition", ENGINEERING IN LIFE SCIENCES, vol. 17, no. 3, March 2017 (2017-03-01), pages 226 - 236, XP055630408 * |
| CHUNG ET AL., PROC. NATL. ACAD. SCI. U.S.A., vol. 86, 1989, pages 2172 |
| FEIGNER, P.L. ET AL., PROC. NATL. ACAD. SCI. U.S.A., vol. 84, 1984, pages 7413 - 7417 |
| GENE, vol. 96, 1990, pages 23 |
| J. AM. OIL CHEM. SOC., vol. 60, 1983, pages 291 - 294 |
| J. AM. OIL CHEM. SOC., vol. 75, 1998, pages 953 - 959 |
| J. MOL. BIOL., vol. 166, 1983, pages 557 |
| J. MOL. BIOL., vol. 53, 1970, pages 159 |
| JOURNAL OF JAPAN OIL CHEMISTS' SOCIETY, vol. 48, 1999, pages 1151 - 1159 |
| KARLINALTSCHUL, PROC. NATL. ACAD. SCI. USA, vol. 87, 1990, pages 2264 - 68 |
| KARLINALTSCHUL, PROC. NATL. ACAD. SCI. USA, vol. 90, 1993, pages 5873 - 77 |
| MEYERSMILLER, COMPUT. APPL. BIOSCI., vol. 4, 1988, pages 11 - 17 |
| OLEOSCIENCE, vol. 6, 2006, pages 145 - 151 |
| SHIMIZU, Y. ET AL., NATURE BIOTECH., vol. 19, 2001, pages 751 - 755 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023116569A1 (en) | 2021-12-21 | 2023-06-29 | Novozymes A/S | Composition comprising a lipase and a booster |
| CN116024196A (zh) * | 2022-11-25 | 2023-04-28 | 广西科学院 | 一种脂肪酶突变体及其应用 |
| WO2024121058A1 (en) | 2022-12-05 | 2024-06-13 | Novozymes A/S | A composition comprising a lipase and a peptide |
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| Publication number | Publication date |
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| CN111684065A (zh) | 2020-09-18 |
| CN111684065B (zh) | 2025-08-19 |
| EP3750991A1 (en) | 2020-12-16 |
| EP3750991A4 (en) | 2021-12-01 |
| JPWO2019155790A1 (ja) | 2021-01-28 |
| US20200370077A1 (en) | 2020-11-26 |
| US11549130B2 (en) | 2023-01-10 |
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