JP2006034165A - Method for producing pqqgdh - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To improve the productivity of PQQGDH, especially holo-form PQQGDH which is an active form, and/or the PQQGDH containing an improved proportion of the holo-form PQQGDH. <P>SOLUTION: The method for producing the recombinant PQQGDH is characterized by the addition of an organic solvent, especially mono-ols to a medium in the production of a recombinant protein by using a host having a PQQ-producing ability. The PQQGDH produced by the method is also provided. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

The present invention relates to a method for producing glucose dehydrogenase (GDH) (hereinafter also abbreviated as PQQGDH) using pyrroloquinoline quinone (PQQ) as a coenzyme, and a glucose sensor using the same. The PQQGDH of the present invention is useful for the determination of glucose in clinical examinations and food analysis.

  PQQGDH is a glucose dehydrogenase using pyrroloquinoline quinone (PQQ) as a coenzyme. Since it catalyzes the reaction of oxidizing glucose to produce gluconolactone, it can be used for blood glucose measurement. Blood glucose concentration is an extremely important index for clinical diagnosis as an important marker of diabetes. Currently, blood glucose concentration is measured mainly by a method using a biosensor using glucose oxidase, but the reaction is affected by the dissolved oxygen concentration, which may cause an error in the measured value. . PQQ-dependent glucose dehydrogenase has attracted attention as a new enzyme that replaces this glucose oxidase.

Our group found that Acinetobacter baumannii NCIMB11517 strain produces PQQ-dependent glucose dehydrogenase, and constructed a gene cloning and expression system (see Patent Document 1). However, it is difficult to say that the productivity is sufficient for industrial use. In particular, from an industrial point of view, there is a need to increase the productivity of holo-type PQQ-dependent glucose dehydrogenase, which is an active form (Patent Document 1 not described) Content).
Japanese Patent Laid-Open No. 11-243949

The present invention has been made against the background of the problems of the prior art, and relates to the improvement of PQQGDH, particularly the improvement of productivity of the active holo-type PQQGDH.

As a result of intensive studies to solve the above problems, the present inventors have finally completed the present invention. That is, the present invention
Item 1.
Item 1. A method for producing recombinant PQQ-dependent glucose dehydrogenase, which comprises adding an organic solvent to a medium in production of a recombinant protein using a host having PQQ production ability.
Recombinant PQQ-dependent glucose dehydrogenase characterized in that in production of a recombinant protein using a host having PQQ-producing ability, the amount of PQQ-dependent glucose dehydrogenase protein produced is improved by adding an organic solvent to the medium. Item 3. Production method
In production of recombinant protein using a host having PQQ production ability, the protein production amount of holo-type PQQ-dependent glucose dehydrogenase is improved by adding an organic solvent to the medium. Item 4. Production Method of Dehydrogenase
In the production of recombinant protein using a host having PQQ production ability, the ratio of holo-type PQQ-dependent glucose dehydrogenase to the total PQQ-dependent glucose dehydrogenase is improved by adding an organic solvent to the medium. Item 5. Method for producing PQQ-dependent glucose dehydrogenase
Item 5. The method for producing a PQQ-dependent glucose dehydrogenase according to any one of Items 1 to 4, wherein the organic solvent is selected from monools.
Item 6. The method for producing a PQQ-dependent glucose dehydrogenase according to any one of Items 1 to 4, wherein the organic solvent is selected from methanol, ethanol, propanol, and butanol.
Item 7. The method according to any one of Items 1 to 6, wherein the holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 45% or more of the total PQQ-dependent glucose dehydrogenase.
Item 8. The method according to any one of Items 1 to 6, wherein the holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 70% or more of the total PQQ-dependent glucose dehydrogenase.
PQQ-dependent glucose dehydrogenase characterized in that, in the production of recombinant protein using a host having PQQ-producing ability, holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 45% or more of the total PQQ-dependent glucose dehydrogenase Item 10. Production method
PQQ-dependent glucose dehydrogenase characterized in that, in the production of a recombinant protein using a host having PQQ-producing ability, holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 70% or more of the total PQQ-dependent glucose dehydrogenase 10. Production method of
Item 11. PQQ-dependent glucose dehydrogenase produced by any one of the methods 1 to 10.
Item 14. A glucose assay kit comprising a PQQ-dependent glucose dehydrogenase produced by the method according to any one of items 1 to 10.
Item 11. A glucose sensor comprising a PQQ-dependent glucose dehydrogenase produced by the method according to any one of Items 1 to 10.
Item 14.
Item 11. A glucose measurement method comprising a PQQ-dependent glucose dehydrogenase produced by the method according to any one of Items 1 to 10.
It is.

The improvement in productivity of PQQGDH according to the present invention, particularly the improvement in productivity as a holo-type PQQGDH, leads to a reduction in manufacturing cost. Furthermore, since the ratio of the holo-type PQQGDH is improved, there is no need to add a PQQ to make an active type PQQGDH to make a holo, which leads to a reduction in manufacturing cost. These make it possible to manufacture PQQGDH at low cost. Furthermore, the glucose assay kit and the glucose sensor can be provided at a low price.

Moreover, since the activity value per unit protein weight of PQQGDH is improved by increasing the ratio of holo-type PQQGDH, it is also possible to reduce the amount of protein added to the glucose assay kit and glucose sensor.

  Hereinafter, the present invention will be described in detail.

PQQGDH used in the present invention is an enzyme that catalyzes a reaction in which pyrroloquinoline quinone is coordinated as a coenzyme to oxidize D-glucose to produce D-glucono-1,5-lactone. The structure is not particularly limited.
At the present time, the cloning of PQQGDH is based on Acinetobacter calcoaceticus LMD 79.41 (AM Cleton-Jansen et al., J. Bacteriol., 170, 2121 (1988) and Mol. Gene. Genet. , 217, 430 (1989)), Escherichia coli (AM Cleton-Jansen et al., J. Bacteriol., 172, 6308 (1990)), Gluconobacter oxydans. ) (Mol. Gen. Genet., 229, 206 (1991)) and Acinetobacter baumannii reported in Patent Document 1 It has been carried out from Acinetobacter baumanni) NCIMB11517. However, it is difficult to modify a membrane enzyme present in Escherichia coli to make it soluble, and it is preferable to select soluble PQQGDH such as Acinetobacter calcoaceticus or Acinetobacter baumannii as the origin. .
Acinetobacter baumannii NCIMB11517 strain was previously classified as Acinetobacter calcaceticus.

  The amino acid sequence of PQQGDH derived from the genus Acinetobacter is preferably the amino acid sequence of PQQGDH derived from Acinetobacter calcoaceticus or Acinetobacter baumannii. Among them, SEQ ID NO: 1 is preferable. The wild-type PQQGDH protein represented by SEQ ID NO: 1 and its base sequence represented by SEQ ID NO: 2 originate from Acinetobacter baumanni NCIMB11517 strain, and are disclosed in JP-A-11-243949 Yes. In the above and SEQ ID NO: 1, the amino acid notation is numbered with 1 aspartic acid from which the signal sequence has been removed.

For example, when the amino acid sequence of SEQ ID NO: 1 is compared with the amino acid sequence of the enzyme derived from Acinetobacter calcoaceticus LMD79.41, the difference is slight and the homology is 92.3% (including the signal sequence). ) And are very similar, it can be easily recognized which amino acid residue of an enzyme of another origin corresponds to a certain residue in SEQ ID NO: 1. These PQQGDHs are also included within the scope of the present invention.

As long as it has glucose dehydrogenase activity, a part of another amino acid residue may be deleted or substituted, and another amino acid residue may be added.

  The prepared DNA having genetic information of the modified protein is transferred into a host microorganism in a state of being linked to a plasmid, and becomes a transformant that produces the modified protein. As the plasmid at this time, for example, pBluescript, pUC18, etc. can be used when Escherichia coli is used as a host microorganism. Examples of host microorganisms that can be used include Escherichia coli W3110, Escherichia coli C600, Escherichia coli JM109, and Escherichia coli DH5α. As a method for transferring the recombinant vector into the host microorganism, for example, when the host microorganism is a microorganism belonging to the genus Escherichia, a method for transferring the recombinant DNA in the presence of calcium ions can be employed. An electroporation method may be used. Furthermore, a commercially available competent cell (for example, competent high JM109; manufactured by Toyobo) may be used.

  Such genes may be extracted from these strains or chemically synthesized. Furthermore, it is possible to obtain a DNA fragment containing the PQQGDH gene by using the PCR method.

  In the present invention, a method for obtaining a gene encoding PQQGDH includes the following methods. For example, after separating and purifying the chromosome of Acinetobacter calcoaceticus NCIB11517, DNA was cleaved using sonication, restriction enzyme treatment, etc., linear expression vector and DNA at the blunt or sticky ends of both DNAs The recombinant vector is constructed by ligation and closing with ligase or the like. After transferring the recombinant vector into a replicable host microorganism, screening is performed using the expression of the vector marker and enzyme activity as an index, and a recombinant vector containing a gene encoding GDH having PQQ as a prosthetic group is retained. To obtain microorganisms.

  Subsequently, the microorganism holding the recombinant vector can be cultured, the recombinant vector can be isolated and purified from the cells of the cultured microorganism, and the gene encoding GDH can be collected from the expression vector. For example, the chromosomal DNA of Acinetobacter calcoaceticus NCIB11517, which is a gene donor, is specifically collected as follows.

  A culture solution obtained by stirring and culturing the gene-donating microorganism for 1 to 3 days, for example, is collected by centrifugation, and then lysed to prepare a GDH gene-containing lysate containing PQQ as a prosthetic group can do. As a method for lysis, for example, treatment is performed with a lytic enzyme such as lysozyme, and a protease, other enzyme, or a surfactant such as sodium lauryl sulfate (SDS) is used in combination as necessary. Further, it may be combined with a physical crushing method such as freeze-thawing or French press treatment.

  In order to separate and purify DNA from the lysate obtained as described above, a conventional method is used, for example, by appropriately combining methods such as deproteinization treatment by phenol treatment or protease treatment, ribonuclease treatment, and alcohol precipitation treatment. be able to.

  A method of cleaving DNA separated and purified from microorganisms can be performed by, for example, ultrasonic treatment, restriction enzyme treatment, or the like. Type II restriction enzymes that act on specific nucleotide sequences are suitable.

  As a vector for cloning, a vector constructed for gene recombination from a phage or plasmid that can autonomously grow in a host microorganism is suitable. Examples of the phage include Lambda gt10 and Lambda gt11 when Escherichia coli is used as a host microorganism. Examples of plasmids include pBR322, pUC19, and pBluescript when Escherichia coli is used as a host microorganism.

  At the time of cloning, a vector fragment can be obtained by cleaving the above-described vector with the restriction enzyme used to cleave the microbial DNA that is the gene donor encoding GDH described above. It is not necessary to use the same restriction enzyme as that used in the above. The method for binding the microbial DNA fragment and the vector DNA fragment may be a method using a known DNA ligase. For example, after annealing of the sticky end of the microbial DNA fragment and the sticky end of the vector fragment, an appropriate DNA ligase is used. A recombinant vector of a microbial DNA fragment and a vector DNA fragment is prepared by use. If necessary, after annealing, it can be transferred to a host microorganism and a recombinant vector can be prepared using in vivo DNA ligase.

  The host microorganism used for cloning is not particularly limited as long as the recombinant vector is stable, can autonomously propagate, and can express a foreign gene. Generally, Escherichia coli W3110, Escherichia coli C600, Escherichia coli HB101, Escherichia coli JM109, Escherichia coli DH5α, and the like can be used.

  As a method for transferring the recombinant vector into the host microorganism, for example, when the host microorganism is Escherichia coli, a competent cell method or an electroporation method using calcium treatment can be used.

  The microorganism which is a transformant obtained as described above can stably produce a large amount of GDH by being cultured in a nutrient medium. The selection of whether or not the target recombinant vector is transferred to the host microorganism may be performed by searching for a microorganism that simultaneously expresses GDH activity by adding a drug resistance marker of the vector holding the target DNA and PQQ. For example, a microorganism that grows in a selective medium based on a drug resistance marker and generates GDH may be selected.

  The base sequence of the GDH gene having PQQ as a prosthetic group obtained by the above method was decoded by the dideoxy method described in Science, Vol. 214, 1205 (1981). The amino acid sequence of GDH was estimated from the base sequence determined as described above.

  As described above, transfer from a recombinant vector having a GDH gene having PQQ selected once as a prosthetic group to a recombinant vector capable of replicating in a microorganism capable of producing PQQ retains the GDH gene. It can be easily carried out by collecting DNA, which is a GDH gene, from a recombinant vector by a restriction enzyme or PCR method and binding it to other vector fragments. Moreover, the transformation of the microorganism which has PQQ production ability by these vectors can use the competent cell method by electrolysis, the electroporation method, etc.

  Examples of microorganisms capable of producing PQQ include methanol-utilizing bacteria such as the genus Methylobacterium, acetic acid bacteria belonging to the genus Acetobacter and Gluconobacter, and the genus Flavobacterium And bacteria such as Pseudomonas and Acinetobacter. Among them, a host-vector system that can use Pseudomonas bacteria and Acinetobacter bacteria is established and is preferable because it is easy to use.

  For Pseudomonas bacteria, Pseudomonas aeruginosa, Pseudomonas fluorescens, Pseudomonas petitida and the like can be used. As Acinetobacter bacteria, Acinetobacter calcoaceticus, Acinetobacter baumannii and the like can be used.

  As a recombinant vector that can be replicated in the microorganism, a vector derived from RSF1010 or a vector having a similar replicon can be used for Pseudomonas bacteria. For example, pKT240, pMMB24, etc. (MM Bagdasarian et al., Gene, 26, 273 (1983)), pCN40, pCN60, etc. (CC Nito et al., Gene, 87, 145 (1990)) and pTS1137 (gene set) Practical technology for replacement, Vol. 4, p73-85, 1983, published by Silence Forum Co., Ltd.). Further, pME290 and the like (Y. Itoh et al., Gene, 36, 27 (1985)), pNI111, pNI20C (N. Itoh et al., J. Biochem., 110, 614 (1991)) can also be used.

  In bacteria belonging to the genus Acinetobacter, pWM43 and the like (W. Minas et al., Appl. Environ. Microbiol., 59, 2807 (1993)), pKT230, pWH1266 and the like (M. Hunger et al., Gene, 87, 45 (1990)) are used as vectors. Is available.

  The microorganism, which is the transformant thus obtained, can produce PQQGDH protein by culturing in a nutrient medium. However, by adding an organic solvent to the medium, productivity as a whole PQQGDH protein can be improved. It is possible to improve productivity as a type PQQGDH protein. The culture form of the host microorganism, which is a transformant, may be selected in consideration of the nutritional physiological properties of the host, and in many cases, the culture is performed in liquid culture. Industrially, aeration and agitation culture is advantageous.

  In the present invention, the holo-type PQQGDH refers to the PQQGDH enzyme itself in which the coenzyme PQQ is bound to the GDH protein and the state thereof, and the enzyme having the GDH activity without the addition of PQQ and the state thereof. On the other hand, the total PQQGDH refers to the total GDH enzyme protein obtained by combining the holo-type PQQGDH and the apo-type PQQGDH in which the coenzyme PQQ is not bound to the GDH protein and the state thereof.

  As a nutrient source of the medium, those commonly used for culturing microorganisms can be widely used. Any carbon compound that can be assimilated may be used as the carbon source. For example, glucose, sucrose, lactose, maltose, lactose, molasses, pyruvic acid and the like are used. The nitrogen source may be any available nitrogen compound. For example, peptone, meat extract, yeast extract, casein hydrolyzate, soybean cake alkaline extract, and the like are used. In addition, phosphates, carbonates, sulfates, salts such as magnesium, calcium, potassium, iron, manganese, and zinc, specific amino acids, specific vitamins, and the like are used as necessary.

  Although the kind and addition amount of an organic solvent are not specifically limited, Preferably they are monools, More preferably, they are methanol, ethanol, and 2-propanol. On the other hand, the addition amount is desirably in the range of 0.1 to 5%, more desirably 0.5 to 2% by volume with respect to the medium.

  In the present invention, monools are a general term for alcohols having one molecule of hydroxyl group in the molecule, and specifically include methanol as a primary alcohol, ethanol and 2-propanol as a secondary alcohol. It is clearly distinguished from diols having two hydroxyl groups in the molecule.

  The culture temperature can be appropriately changed within the range in which the bacteria grow and produce PQQGDH, but in the case of the microorganism having the PQQ production ability as described above, it is preferably 20 to 42 ° C, more preferably about 30 to 37 ° C. . Although the culture time varies slightly depending on the conditions, the culture may be completed at an appropriate time in consideration of the time when PQQGDH reaches the maximum yield, and is usually about 6 to 48 hours, preferably about 16 to 36 hours. The pH of the medium can be appropriately changed within the range in which the bacteria grow and produce PQQGDH, but is preferably about pH 6.0 to 9.0, more preferably pH 6.5 to 8.0.

  Although the culture solution containing the microbial cells producing PQQGDH in the culture can be collected and used as it is, generally, when PQQGDH is present in the culture solution, filtration, centrifugation, etc. It is used after separating the PQQGDH-containing solution and microbial cells. When PQQGDH is present in the microbial cells, the microbial cells are collected from the obtained culture by means of filtration or centrifugation, and then the microbial cells are destroyed by a mechanical method or an enzymatic method such as lysozyme. Further, if necessary, a chelating agent such as EDTA and a surfactant are added to solubilize GDH and separated and collected as an aqueous solution.

  The PQQGDH-containing solution obtained as described above is precipitated by, for example, vacuum concentration, membrane concentration, salting-out treatment with ammonium sulfate, sodium sulfate or the like, or fractional precipitation with a hydrophilic organic solvent such as methanol, ethanol, acetone, etc. You just have to let them know. Heat treatment and isoelectric point treatment are also effective purification means. Thereafter, purified PQQGDH can be obtained by performing gel filtration with an adsorbent or gel filter, adsorption chromatography, ion exchange chromatography, and affinity chromatography.

  For example, separation and purification by gel filtration using Sephadex gel (Pharmacia Biotech), column chromatography such as DEAE Sepharose CL-6B (Pharmacia Biotech), octyl Sepharose CL-6B (Pharmacia Biotech), etc. Goods can be obtained. The purified enzyme preparation is preferably purified to the extent that it shows a single band on electrophoresis (SDS-PAGE).

  The purified enzyme obtained as described above can be pulverized and distributed, for example, by freeze drying, vacuum drying, spray drying, or the like. At this time, the purified enzyme may be one dissolved in a phosphate buffer, a Tris-HCl buffer, or a GOOD buffer. Preferred are GOOD buffers, with PIPES, MES or MOPS buffers being particularly preferred. Moreover, PQQGDH can be further stabilized by adding calcium ions or salts thereof, amino acids such as glutamic acid, glutamine, and lysine, and serum albumin.

  The PQQGDH protein can take various forms such as liquid (aqueous solution, suspension, etc.), powder, and lyophilized. The lyophilization method is not particularly limited and may be performed according to a conventional method. The composition containing the enzyme of the present invention is not limited to a lyophilized product, and may be in a solution state in which the lyophilized product is redissolved. Moreover, when measuring glucose, various forms, such as a glucose assay kit and a glucose sensor, can be taken. The purified modified protein thus obtained can be stabilized by the following method.

  (1) One or more compounds selected from the group consisting of (1) aspartic acid, glutamic acid, α-ketoglutaric acid, malic acid, α-ketogluconic acid, α-cyclodextrin, and salts thereof And (2) By coexisting albumin, the modified protein can be further stabilized.

  In the lyophilized composition, the PQQGDH content varies depending on the origin of the enzyme, but is usually suitably used in the range of about 5 to 50% (weight ratio). When converted into enzyme activity, it is preferably used in the range of 100 to 2000 U / mg.

  Examples of salts of aspartic acid, glutamic acid, α-ketoglutaric acid, malic acid, and α-ketogluconic acid include salts of sodium, potassium, ammonium, calcium, magnesium, and the like, but are not particularly limited. The addition amount of the above compound, its salt and α-cyclodextrin is preferably in the range of 1 to 90% (weight ratio). These substances may be used alone or in combination.

  The buffer solution to be contained is not particularly limited, and examples thereof include Tris buffer solution, phosphate buffer solution, borate buffer solution, and GOOD buffer solution. The pH of the buffer is adjusted in the range of about 5.0 to 9.0 according to the purpose of use. The content of the buffering agent in the lyophilized product is not particularly limited, but is preferably 0.1% (weight ratio) or more, particularly preferably 0.1 to 30% (weight ratio). used.

  Examples of albumin that can be used include bovine serum albumin (BSA) and ovalbumin (OVA). BSA is particularly preferable. The content of the albumin is preferably 1 to 80% (weight ratio), more preferably 5 to 70% (weight ratio).

  Further, other stabilizers and the like may be added to the composition within a range that does not particularly adversely affect the reaction of PQQGDH. The blending method of the stabilizer of the present invention is not particularly limited. For example, a method of blending a stabilizer in a buffer solution containing PQQGDH, a method of blending PQQGDH in a buffer solution containing a stabilizer, or a method of blending PQQGDH and a stabilizer in a buffer solution at the same time can be mentioned.

  Moreover, the stabilization effect is acquired even if calcium ion is added. That is, the modified protein can be stabilized by containing calcium ions or calcium salts. Examples of calcium salts include calcium chloride, calcium salts of inorganic acids such as calcium acetate and calcium citrate, and organic acids. In the aqueous composition, the calcium ion content is preferably 1 × 10 −4 to 1 × 10 −2 M.

  The stabilizing effect by containing calcium ions or calcium salts is further improved by containing an amino acid selected from the group consisting of glutamic acid, glutamine and lysine.

  One or more amino acids selected from the group consisting of glutamic acid, glutamine and lysine may be used. In the aqueous composition, the content of an amino acid selected from the group consisting of glutamic acid, glutamine and lysine is preferably 0.01 to 0.2% by weight.

  Further, serum albumin may be contained. When serum albumin is added to the aqueous composition, the content is preferably 0.05 to 0.5% by weight.

  As a buffering agent, a normal thing is used, and what makes pH of a composition 5-10 normally is preferable. Specifically, Tris-HCl, boric acid, and Good's buffer are used, but any buffer that does not form an insoluble salt with calcium can be used.

  If necessary, other components such as surfactants, stabilizers and excipients may be added to the aqueous composition.

In the present invention, glucose can be measured by the following various methods.
Glucose Assay Kit The present invention also features a glucose assay kit comprising PQQGDH according to the present invention. The glucose assay kit of the present invention comprises PQQGDH according to the present invention in an amount sufficient for at least one assay. Typically, the kit contains the PQQGDH of the present invention, plus the buffers necessary for the assay, mediators, glucose standard solution for creating a calibration curve, and directions for use. The PQQGDH according to the present invention can be provided in various forms, for example, as a lyophilized reagent or as a solution in a suitable storage solution. Preferably, the PQQGDH of the present invention is provided in a holified form, but may be provided in the form of an apoenzyme and holified at the time of use.

Glucose Sensor The present invention also features a glucose sensor that uses PQQGDH according to the present invention. As the electrode, a carbon electrode, a gold electrode, a platinum electrode or the like is used, and the enzyme of the present invention is immobilized on this electrode. Immobilization methods include a method using a crosslinking reagent, a method of encapsulating in a polymer matrix, a method of coating with a dialysis membrane, a photocrosslinkable polymer, a conductive polymer, a redox polymer, etc., or ferrocene or a derivative thereof. It may be fixed in a polymer or adsorbed and fixed on an electrode together with a representative electron mediator, or a combination thereof may be used. Preferably, the PQQGDH of the present invention is immobilized on the electrode in a holographic form, but it can also be immobilized in the form of an apoenzyme and the PQQ provided as a separate layer or in solution. Typically, PQQGDH of the present invention is immobilized on a carbon electrode using glutaraldehyde and then treated with a reagent having an amine group to block glutaraldehyde.

The glucose concentration can be measured as follows. The buffer is placed in a thermostatic cell, and PQQ and CaCl ₂ and mediator are added to maintain a constant temperature. As the mediator, potassium ferricyanide, phenazine methosulfate, or the like can be used. An electrode on which the PQQGDH of the present invention is immobilized is used as a working electrode, and a counter electrode (for example, a platinum electrode) and a reference electrode (for example, an Ag / AgCl electrode) are used. After a constant voltage is applied to the carbon electrode and the current becomes steady, a sample containing glucose is added and the increase in current is measured. The glucose concentration in the sample can be calculated according to a calibration curve prepared with a standard concentration glucose solution.

Examples of producing PQQ or an enzyme using PQQ as a coenzyme by culturing a microorganism having PQQ-producing ability in a medium to which an organic solvent has been added include Patent Document 2 and Non-Patent Document 1. Patent Document 2 describes contents of PQQ accumulating in a culture solution by culturing a methanol-assimilating bacterium having confirmed PQQ production ability in a medium containing methanol as a main carbon source. Further, in Non-Patent Document 1, microorganisms having various PQQ production ability were cultured using an organic solvent or the like as a carbon source, and by adding some methanol or the like with some microorganisms, the carbon source was used as a substrate for PQQ. The content that the productivity of methanol dehydrogenase and alcohol dehydrogenase using as a coenzyme has been confirmed is described.
However, these examples only describe that PQQ production and enzyme production using the organic solvent as a substrate were confirmed when culturing using an organic solvent such as methanol as a carbon source. As described in Non-Patent Document 1, methanol or the like is not essential for the production of enzymes and PQQ using it as a substrate (enzymes and PQQ can exist even in the absence of an organic solvent). In addition, there is no direct report that the productivity of an enzyme using an organic solvent as a substrate and PQQ as a coenzyme has been improved. Furthermore, there is no report that the addition of an organic solvent to the medium has improved the productivity of glucose dehydrogenase that is not a substrate or a different metabolic system, and the glucose dehydrogenase was introduced from outside by genetic recombination. In this case, there is no report that the productivity of glucose dehydrogenase with different metabolic system is improved by adding an organic solvent to the medium.
From this point of view, in the present recombinant production using a host having PQQ production ability, the productivity of glucose dehydrogenase, which is irrelevant to the organic solvent as a substrate, is cultured by culturing in a medium to which an organic solvent is added. It was surprising that improved. Further, even if the host PQQ productivity may be improved by adding an organic solvent to the medium, a host PQQ-dependent enzyme (for example, methanol dehydrogenase in the case of methanol) using an organic solvent as a substrate at the same time may be used. ) Will also improve, the productivity of glucose dehydrogenase as the amount of protein will increase as the result of the increase in the productivity of glucose dehydrogenase. It was a completely unexpected event that not only the improvement but also the ratio as a holo type was improved.
JP 5-10077 APPLIED AND ENVIRONMENTAL MICROBIOLOGY, May 1989, p1209-1213

Hereinafter, the present invention will be described in more detail based on examples.
Example 1: Construction of PQQ-dependent glucose dehydrogenase gene expression plasmid The wild-type PQQ-dependent glucose dehydrogenase expression plasmid pNPG5 was transformed into the multiple cloning site of the vector pBluescript SK (-) at Acinetobacter baumannii. A structural gene encoding a PQQ-dependent glucose dehydrogenase derived from NCIMB11517 strain is inserted. The base sequence is shown in SEQ ID NO: 2 in the sequence listing, and the amino acid sequence of PQQ-dependent glucose dehydrogenase deduced from the base sequence is shown in SEQ ID NO: 1 in the sequence listing.

Example 2: Construction of an expression vector capable of replicating in Pseudomonas bacteria 5 μg of the recombinant plasmid pNPG5 DNA obtained in Example 1 was cleaved with restriction enzymes BamHI and XHoI (manufactured by Toyobo Co., Ltd.) to obtain a PQQ-dependent glucose dehydrogenase. The structural gene part was isolated. The isolated DNA and pTS1137 (1 μg) cleaved with BamHI and XHoI were reacted with 1 unit of T4 DNA ligase at 16 ° C. for 16 hours to ligate the DNA. Ligated DNA was transformed with Escherichia coli DH5α competent cells. The resulting expression plasmid was named pNPG6.

Example 3 Production of Pseudomonas Bacterium Transformant Pseudomonas putida TE3493 (Microtechnology 12298) was cultured at 30 ° C. for 16 hours in LBG medium (LB medium + 0.3% glycerol) and centrifuged (12 The bacterial cells were collected by 2,000 rpm for 10 minutes, and 8 ml of 5 mM K-phosphate buffer (pH 7.0) containing 300 mM sucrose ice-cooled was added to the bacterial cells to suspend the bacterial cells. The bacterial cells were collected again by centrifugation (12,000 rpm, 10 minutes), and 0.4 ml of 5 mM K-phosphate buffer (pH 7.0) containing 300 mM sucrose ice-cooled was added to the bacterial cells. Suspended.
0.5 μg of the expression plasmid pNPG6 obtained in Example 2 was added to the suspension and transformed by electroporation. A target transformant was obtained from a colony grown on an LB agar medium containing 100 μg / ml streptomycin.

Test example 1
Method for measuring the activity of holo-type PQQGDH Measurement principle D-glucose + PMS + PQQGDH → D-glucono-1,5-lactone + PMS (red)
The presence of diformazan formed by the reduction of nitrotetrazolium blue (NTB) by 2PMS (red) + NTB → 2PMS + diformazan phenazine methosulfate (PMS) (red) was measured spectrophotometrically at 570 nm.
Definition of Unit One unit refers to the amount of PQQGDH enzyme that forms 0.5 mmol of diformazan per minute under the conditions described below.
(3) Method reagents A. D-glucose solution: 0.5 M (0.9 g D-glucose (molecular weight 180.16) / 10 ml H ₂ O)
B. PIPES-NaOH buffer, pH 6.5: 50 mM (1.51 g of PIPES (molecular weight 302.36) suspended in 60 mL of water is dissolved in 5N NaOH and 2.2 ml of 10% Triton X-100 is added. The pH was adjusted to 6.5 ± 0.05 at 25 ° C. using 5N NaOH, and water was added to make 100 ml.)
C. PMS solution: 3.0 mM (9.19 mg phenazine methosulfate (molecular weight 817.65) / 10 ml H ₂ O)
D. NTB solution: 6.6 mM (53.96 mg of nitrotetrazolium blue (molecular weight 817.65) / 10 ml H ₂ O)
E. Enzyme dilution: 50 mM PIPES-NaOH buffer (pH 6.5) containing 1 mM CaCl ₂ , 0.1% Triton X-100, 0.1% BSA
Procedure Prepare the following reaction mixture in a light-proof bottle and store on ice (prepared at the time of use)
1.8 ml D-glucose solution (A)
24.6 ml PIPES-NaOH buffer (pH 6.5) (B)
2.0ml PMS solution (C)
1.0ml NTB solution (D)

3.0 ml of the reaction mixture was placed in a test tube (made of plastic) and preheated at 37 ° C. for 5 minutes.
0.1 ml enzyme solution was added and mixed by gentle inversion.
The increase in absorbance for water at 570 nm was recorded for 4-5 minutes on a spectrophotometer while maintaining at 37 ° C., and ΔOD per minute from the initial linear portion of the curve was calculated (OD test).
At the same time, the same method was repeated except that the enzyme diluent (E) was added instead of the enzyme solution, and a blank (ΔOD blank) was measured.
Immediately before the assay, the enzyme powder was dissolved in an ice-cold enzyme diluent (E) and diluted to 0.1-0.8 U / ml with the same buffer (use of a plastic tube for adhesion of the enzyme) Is preferred).
Calculation Activity is calculated using the following formula:
U / ml = {ΔOD / min (ΔOD test−ΔOD blank) × Vt × df} / (20.1 × 1.0 × Vs)
U / mg = (U / ml) × 1 / C
Vt: Total volume (3.1 ml)
Vs: Sample volume (1.0 ml)
20.1: 1/2 mmol molecular extinction coefficient of diformazan 1.0: optical path length (cm)
df: Dilution factor C: Enzyme concentration in solution (c mg / ml)

Test example 2
Method for measuring activity of total PQQGDH In Test Example 1, instead of enzyme diluent (E), enzyme diluent (F): 1 mM CaCl ₂ , 0.1% Triton X-100, 0.1% BSA, 1 μM PQQ After the enzyme was diluted with 50 mM PIPES-NaOH buffer (pH 6.5), the same measurement was performed.

Example 4 Confirmation that PQQ productivity is rate-limiting in PQQGDH expression 25 ml of GDH production medium (1.5% glycerol, 4% yeast extract, 1.25% K2HPO4, 0.23% KH2PO4, pH 6.8) ) Was dispensed into a 500 ml Sakaguchi flask and autoclaved at 121 ° C. for 20 minutes to sterilize the medium. After standing to cool, separately sterile filtered streptomycin was added to a concentration of 100 μg / ml. Separately, 5 ml of supplemental medium (16.8% glycerol, 4.8% yeast extract) was prepared and sterilized in the same manner. The transformant obtained in Example 3 was cultured with shaking in a GDH production medium at 33 ° C., and after 16 hours, 5 ml of supplemented medium was added, and the culture was continued. After culturing for 24 hours, centrifugation ( The cells were collected at 12000 rpm for 5 minutes. As a control, culture without supplemental medium was also performed. The cells are suspended in 20 mM phosphate buffer (pH 7.0), crushed by sonication, and further centrifuged to obtain a supernatant as a crude enzyme solution. PQQGDH is obtained according to Test Examples 1 and 2. Activity was measured. The measurement results are shown in Table 2.

In the results of Example 4, the activity of the total enzyme PQQGDH in the crude enzyme solution was significantly improved by the addition of the supplement medium, whereas the activity of the holo-type PQQGDH was slightly improved. . This phenomenon indicates that in the production of PQQGDH, the productivity of coenzyme PQQ is rate-limiting for the improvement in the productivity of GDH protein. In the production of PQQGDH, it is necessary to improve the productivity of coenzyme PQQ. Represents something.

Example 5 Comparison of PQQGDH expression level of transformant by addition of organic solvent to medium 25 ml of GDH production medium (1.5% glycerol, 4% yeast extract, 1.25% K2HPO4, 0.23% KH2PO4, pH 6. 8) was dispensed into a 500 ml Sakaguchi flask, autoclaved at 121 ° C. for 20 minutes, and the medium was sterilized. After standing to cool, separately sterile filtered streptomycin was added to a concentration of 100 μg / ml. Separately, 5 ml of supplemental medium (16.8% glycerol, 4.8% yeast extract) was prepared, sterilized in the same manner, allowed to cool, and then 0.25 ml of the organic solvent used for the study was added. As a control, a supplemental medium not added with an organic solvent was prepared at the same time, and 0.25 ml of sterilized water was added to correct the liquid amount. The transformant obtained in Example 3 was cultured with shaking in a GDH production medium at 33 ° C. After 16 hours, 5.25 ml of supplemented medium was added, and the culture was continued. After culturing for 24 hours, centrifugation was performed. The cells were collected by separation (12000 rpm, 5 minutes). The cells are suspended in 20 mM phosphate buffer (pH 7.0), crushed by sonication, and further centrifuged to obtain a supernatant as a crude enzyme solution. PQQGDH is obtained according to Test Examples 1 and 2. Activity was measured. Productivity was calculated by dividing the PQQGDH activity (U / ml) per unit culture volume by the culture turbidity (OD660) at the end of the culture, and converting it to a unit cell mass conversion (U / ml / OD660). The ratio of the expression level of holo-type PQQGDH was calculated by dividing the holo-type PQQGDH activity (U / ml) expressed per unit liquid volume by the total PQQGDH activity (U / ml). Since the PQQGDH activity and the amount of PQQGDH protein have a positive correlation such that if the amount of PQQGDH protein doubles, the PQQGDH activity also doubles, the improvement in PQQGDH productivity is the amount of PQQGDH protein production Synonymous with improvement. The measurement results are shown in Table 3, and the calculation results are shown in Table 4.

The addition of organic solvents, especially monools, to the medium not only confirms further improvement in GDH protein productivity beyond medium addition, but also increases holo-type PQQGDH productivity, which seems to be due to the improvement in PQQ productivity. Significant improvement was observed, and the ratio of the expression level of holo-type PQQGDH compared with no addition of organic solvent was also greatly improved.

According to the present invention, it is possible to improve productivity as PQQGDH, particularly as a holo type PQQGDH, and to manufacture PQQGDH at low cost. Furthermore, the glucose assay kit and the glucose sensor can be provided at a low price. On the other hand, the activity value per unit protein weight of PQQGDH is improved by increasing the ratio of holo-type PQQGDH. PQQGDH is preferable for use because it allows a reduction in the amount of protein added to the glucose assay kit and glucose sensor.

Claims (14)

A method for producing a recombinant PQQ-dependent glucose dehydrogenase characterized in that an organic solvent is added to a medium in production of a recombinant protein using a host having PQQ production ability Recombinant PQQ-dependent glucose dehydrogenase characterized in that in production of a recombinant protein using a host having PQQ-producing ability, the amount of PQQ-dependent glucose dehydrogenase protein produced is improved by adding an organic solvent to the medium. Production method In production of recombinant protein using a host having PQQ production ability, the protein production amount of holo-type PQQ-dependent glucose dehydrogenase is improved by adding an organic solvent to the medium. Method for producing dehydrogenase In the production of recombinant protein using a host having PQQ production ability, the ratio of holo-type PQQ-dependent glucose dehydrogenase to the total PQQ-dependent glucose dehydrogenase is improved by adding an organic solvent to the medium. For producing PQQ-dependent glucose dehydrogenase The method for producing a PQQ-dependent glucose dehydrogenase according to any one of claims 1 to 4, wherein the organic solvent is selected from monools. The method for producing a PQQ-dependent glucose dehydrogenase according to any one of claims 1 to 4, wherein the organic solvent is selected from methanol, ethanol, propanol, and butanol. The method according to any one of claims 1 to 6, wherein the holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 45% or more of the total PQQ-dependent glucose dehydrogenase. The method according to any one of claims 1 to 6, wherein the holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 70% or more of the total PQQ-dependent glucose dehydrogenase. PQQ-dependent glucose dehydrogenase characterized in that, in the production of recombinant protein using a host having PQQ-producing ability, holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 45% or more of the total PQQ-dependent glucose dehydrogenase Production method PQQ-dependent glucose dehydrogenase characterized in that, in the production of a recombinant protein using a host having PQQ-producing ability, holo-type PQQ-dependent glucose dehydrogenase is produced at a ratio of 70% or more of the total PQQ-dependent glucose dehydrogenase Production method PQQ-dependent glucose dehydrogenase produced by the method according to any one of claims 1 to 10. A glucose assay kit comprising a PQQ-dependent glucose dehydrogenase produced by the method according to any one of claims 1 to 10. A glucose sensor comprising a PQQ-dependent glucose dehydrogenase produced by the method according to claim 1. The glucose measuring method containing the PQQ dependence glucose dehydrogenase produced by the method in any one of Claims 1-10.