CORYNEFORM BACTERIUM TRANSFORMANT AND PROCESS FOR PRODUCING PHENOL USING THE SAME
The present invention relates to a technique for producing phenol. In more detail, the present invention relates to a coryneform bacterium transformant constructed by specific gene recombination and thereby provided with a phenol-producing function, and relates to an efficient phenol-producing process using the transformant. Against the backdrop of global warming and exhaustion of fossil resources, production of chemical products using renewable resources, along with production of biofuels, is recognized as an emerging industry, biorefinery, which is an important means for realizing a low-carbon society, and has attracted keen attention. However, production of biophenol using renewable resources is less productive as compared to production of lactic acid or ethanol because the metabolic reaction from a raw material saccharide consists of a great many steps. In addition, for the reasons that produced phenol inhibits bacterial proliferation and that phenol is cytotoxic, industrial production of phenol has been considered to be impossible. Important use of phenol is phenol resins. A phenol resin, which is produced by addition condensation of phenol and aldehyde, is one of the oldest plastics, and with its properties including excellent heat resistance and durability, is used for various purposes, such as an alternative automotive material to metal, a semiconductor seal material, and a circuit board even today. Due to extremely high reactivity of phenol and aldehyde as raw materials and to the complicated three-dimensional network structure of resulting phenol resin polymers, precise structural designing and development into nanomaterials thereof had been considered difficult and so had been application to high-value-added use. However, in recent years, the theory of physical-properties of polymers and the simulation thereof have rapidly developed, and therefore it has gradually become possible to create highly functional materials from phenol resins by refining the network structure. Under the circumstances, the phenol resin production in Japan is also increasing year by year. The currently employed industrial production process of phenol (cumene process) is a typical energy-consumptive process in the chemical industry using petroleum-derived benzene and propylene as raw materials, and requiring great amounts of solvent and thermal energy. Therefore, in the light of global environment conservation and greenhouse gas reduction, there is an urgent need to develop an environment-conscious, energy saving process that allows production of phenol from renewable resources and can reduce carbon dioxide emissions and waste products, that is, to establish biophenol production technologies. There have not been reported phenol-producing bacteria in nature so far. Also, there have not been known recombinant bacteria-based phenol-producing technologies to achieve a practically sufficient phenol productivity. Tyrosine phenol-lyase is an enzyme that catalyzes synthesis of tyrosine from phenol, pyruvic acid, and ammonia and the reverse reaction thereof (for example, PTL 1). PTL 2, for example, teaches synthesis of tyrosine from phenol, pyruvic acid, and ammonia with the use of tyrosine phenol-lyase derived from members of the family Enterobacteriaceae. Also, it is known that efficient tyrosine phenol-lyase production can be achieved by transformation of An object of the present invention is to provide a microorganism capable of efficiently producing phenol from tyrosine, and a process for efficiently producing phenol from tyrosine. The present inventors have wholeheartedly carried out investigations in order to achieve the object described above and obtained the following findings. (i) A transformant constructed by transferring a tyrosine phenol-lyase gene into a coryneform bacterium can efficiently produce phenol from tyrosine.
The present invention, which has been completed based on the above-mentioned findings, provides the following transformant and process for producing phenol. [1] A phenol-producing transformant constructed by transferring a gene which encodes an enzyme having tyrosine phenol-lyase activity into a coryneform bacterium as a host.
With the use of the transformant of the present invention, phenol can be efficiently produced from tyrosine. Generally, growth of microorganisms is inhibited by a solvent, such as a phenol, because of its cytotoxicity, and therefore phenol production with the use of microorganisms was difficult. According to the process of the present invention, however, phenol production with the use of microorganisms can be achieved with a practically sufficient efficiency. Hereinafter, the present invention will be described in detail. The transformant of the present invention capable of producing phenol is a transformant constructed by transferring a gene which encodes an enzyme having tyrosine phenol-lyase activity into a coryneform bacterium as a host. The coryneform bacterium is a group of microorganisms defined in Bergey's Manual of Determinative Bacteriology, Vol. 8, 599 (1974), and is not particularly limited as long as it proliferates under normal aerobic conditions. The specific examples include Examples of the Inter alia, According to molecular biological classification, names of some species of coryneform bacteria, such as Examples of the Examples of the Examples of the Examples of the The coryneform bacteria may be, let alone a wild strain, a mutant thereof or an artificial recombinant thereof. Examples thereof include disruptants in which a gene of lactate dehydrogenase, phosphoenolpyruvate carboxylase, or malate dehydrogenase is disrupted. Using such a disruptant as a host can improve phenol productivity and reduce production of by-products. Inter alia, preferred is a disruptant in which a lactate dehydrogenase gene is disrupted. In the disruptant, the lactate dehydrogenase gene is disrupted and the metabolic pathway from pyruvic acid to lactic acid is blocked. Inter alia, especially preferred is a disruptant of Such a disruptant can be prepared based on a conventional gene engineering process. Such a lactate dehydrogenase disruptant and the preparation process thereof are described in WO 2005/010182 A1. As shown in Example 3, the present inventors found that coryneform bacteria have significantly higher resistance to phenol as compared with other microorganisms. In this regard, coryneform bacteria are preferred in the production of phenol by the process of the present invention. In addition, as compared with other aerobic microorganisms, coryneform bacteria can more efficiently produce substances under reducing conditions where the bacteria do not substantially proliferate. In this regard also, coryneform bacteria are preferred in the production of phenol by the process of the present invention. Tyrosine Phenol-Lyase Gene (tpl) Tyrosine phenol-lyase is an enzyme that catalyzes a reaction in which phenol is produced by elimination of pyruvic acid and ammonia from tyrosine and the reverse reaction thereof. Tyrosine phenol-lyase also catalyzes a reaction in which L-DOPA is produced from catechol and pyruvic acid. The gene which encodes an enzyme having tyrosine phenol-lyase activity may be of any origin without particular limitation, and preferred are a gene derived from Examples of the gene derived from In the present invention, a DNA which hybridizes to a DNA consisting of a complementary base sequence of the base sequence of SEQ ID NO: 16, 23, 24, 25, 26, or 27 under stringent conditions and which encodes a polypeptide having tyrosine phenol-lyase activity can also be used. The “stringent conditions” as used herein means general conditions, for example, the conditions described in Molecular Cloning, A Laboratory Manual, Second edition, 1989, Vol. 2, p. 11. 45. It means, in particular, conditions where hybridization occurs at a temperature 5 to 10° C. below the melting temperature (Tm) of a perfect hybrid. The tyrosine phenol-lyase activity can be measured by a modified method of the method described in J. Biol. Chem., 245, 1767-1772 (1970) “Materials and Methods”. Briefly, by adding the test enzyme to a liquid for testing, a reaction mixture containing 50 mM potassium phosphate buffer at pH 8.0, 2.5 mM L-Tyr, 0.1 mM pyridoxal phosphate, 20% glycerol, and the enzyme was prepared, and the mixture was allowed to react at 30° C. for 30 minutes (0, 5, 10, 20, 30 minutes). The reaction was stopped by the addition of 0.6 N hydrochloric acid (final concentration). After the reaction mixture was subjected to centrifugation and filter filtration, the produced phenol was analyzed and quantified by HPLC (Cosmosil C18 ARII, mobile phase: 20% MeOH and 0.07% perchloric acid). The specific activity was calculated based on the initial rate of the reaction and the protein concentration (the amount of the enzyme required to produce 1 μmol of phenol per minute was defined as 1 unit). In the present invention, a DNA consisting of a base sequence which has 90% or more, preferably 95% or more, more preferably 98% or more homology with the base sequence of SEQ ID NO: 16, 23, 24, 25, 26, or 27 and which encodes a polypeptide having tyrosine phenol-lyase activity can also be used. In the present invention, the base sequence homology was calculated using GENETYX Ver. 8 (made by Genetyx). The homolog of the DNA consisting of the base sequence of SEQ ID NO: 16, 23, 24, 25, 26, or 27 can be selected from a DNA library of a different species by, for example, PCR or hybridization using a primer or a probe designed based on these base sequences, according to a conventional method, and as a result, a DNA which encodes a polypeptide having tyrosine phenol-lyase activity can be obtained with a high probability. The DNA which encodes tyrosine phenol-lyase is amplified by PCR and then cloned into a suitable vector which is replicable in a host. The plasmid vector may be any plasmid vector as long as it comprises a gene responsible for autonomously replicating function in a coryneform bacterium. Specific examples of the plasmid vector include pAM330 derived from Examples of a preferred promoter include promoter PgapA as a promoter of the glyceraldehyde-3-phosphate dehydrogenase A gene (gapA), promoter Pmdh as a promoter of the malate dehydrogenase gene (mdh), and promoter PldhA as a promoter of lactate dehydrogenase A gene (ldhA), all of which are derived from Examples of a preferred terminator include terminator rrnB T1T2 of As a method of transformation, any publicly known method can be used without limitation. Examples of such a known method include the calcium chloride/rubidium chloride method, the calcium phosphate method, DEAE-dextran transfection, and electroporation. Inter alia, preferred for a coryneform bacterium is electroporation, which can be performed by a known method (Kurusu, Y. et al., Electroporation-transformation system for Coryneform bacteria by auxotrophic complementation., Agric. Biol. Chem. 54:443-447 (1990); and Vertes A. A. et al., Presence of mrr- and mcr-like restriction systems in Coryneform bacteria. Res. Microbiol. 144:181-185 (1993)). The transformant is cultured using a culture medium usually used for culture of microorganisms. The culture medium may be a natural or synthetic medium containing a carbon source, a nitrogen source, inorganic salts, other nutritional substances, etc. Examples of the carbon source include carbohydrates and sugar alcohols such as glucose, fructose, sucrose, mannose, maltose, mannitol, xylose, arabinose, galactose, starch, molasses, sorbitol and glycerol; organic acids such as acetic acid, citric acid, lactic acid, fumaric acid, maleic acid and gluconic acid; and alcohols such as ethanol and propanol. Hydrocarbons, such as normal paraffin, etc. may also be used as desired. These carbon sources may be used alone or as a mixture of two or more thereof. The concentration of these carbon sources in the culture medium is usually about 0.1 to 10 w/v %. Examples of the nitrogen source include inorganic or organic ammonium compounds, such as ammonium chloride, ammonium sulfate, ammonium nitrate, and ammonium acetate; urea; aqueous ammonia; sodium nitrate; and potassium nitrate. Nitrogen-containing organic compounds, such as corn steep liquor, meat extract, peptone, N—Z-amine, protein hydrolysate, amino acid, etc. may also be used. These nitrogen sources may be used alone or as a mixture of two or more thereof. The concentration of these nitrogen sources in the culture medium varies depending on the kind of the nitrogen compound, but is usually about 0.1 to 10 w/v %. Examples of the inorganic salts include potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium sulfate, sodium chloride, iron(II) nitrate, manganese sulfate, zinc sulfate, cobalt sulfate, and calcium carbonate. These inorganic salts may be used alone or as a mixture of two or more thereof. The concentration of the inorganic salts in the culture medium varies depending on the kind of the inorganic salts, but is usually about 0.01 to 1 w/v %. Examples of the nutritional substances include meat extract, peptone, polypeptone, yeast extract, dry yeast, corn steep liquor, skim milk powder, defatted soybean hydrochloric acid hydrolysate, and extract from animals, plants or microorganisms, and degradation products thereof. The concentration of the nutritional substances in the culture medium varies depending on the kind of the nutritional substances, but is usually about 0.1 to 10 w/v %. Further, vitamins may be added as needed. Examples of the vitamins include biotin, thiamine (vitamin B1), pyridoxine (vitamin B6), pantothenic acid, inositol, nicotinic acid, etc. The pH of the culture medium is preferably about 5 to 8. Examples of the preferable microbial culture medium include A medium (Inui, M. et al., Metabolic analysis of The culture temperature is about 15 to 45° C., and the culture period is about 1 to 7 days. In the coryneform bacterium as a host, the gene which encodes an enzyme having phenol 2-monooxygenase activity (poxF) on the chromosome preferably has a disruption or deletion for further efficient phenol production. Replacement of a gene on the chromosome with the corresponding gene having an disruption or deletion can be achieved by creating a gene with deletion mutation for not allowing production of a normally functioning enzyme protein, and transforming a bacterium with a DNA comprising the mutated gene for recombination in which the gene on the chromosome and the mutated gene are exchanged. An enzyme protein encoded by a gene having a disruption or deletion, even when produced, has a conformation different from that of the wild type, and has no or reduced function. The gene deletion or gene disruption by way of such gene replacement through homologous recombination has already been established, and examples thereof include a method using a plasmid containing a temperature sensitive replication origin or a plasmid capable of conjugal transfer, and a method using a suicide vector not having a replication origin that works in a host (U.S. Pat. No. 6,303,383 and JP 05-007491 A). Specifically, by the method described in Example 1, a coryneform bacterium in which the phenol 2-monooxygenase gene (poxF) is disrupted or deleted can be obtained. Phenol can be produced by a process comprising a step of allowing the above-described transformant of the present invention to react in a reaction mixture containing tyrosine, and a step of collecting phenol from the reaction mixture. Before the reaction, the transformant is preferably cultured and proliferated under aerobic conditions at about 25 to 38° C. for about 12 to 48 hours. The culture medium used for aerobic culture of the transformant before the reaction may be a natural or synthetic medium containing a carbon source, a nitrogen source, inorganic salts, other nutritional substances, etc. Examples of the carbon source that can be used include saccharides (monosaccharides such as glucose, fructose, mannose, xylose, arabinose, and galactose; disaccharides such as sucrose, maltose, lactose, cellobiose, xylobiose, and trehalose; polysaccharides such as starch; and molasses); sugar alcohols such as mannitol, sorbitol, xylitol, and glycerol; organic acids such as acetic acid, citric acid, lactic acid, fumaric acid, maleic acid and gluconic acid; alcohols such as ethanol and propanol; and hydrocarbons such as normal paraffin. These carbon sources may be used alone or as a mixture of two or more thereof. Examples of the nitrogen source that can be used include inorganic or organic ammonium compounds, such as ammonium chloride, ammonium sulfate, ammonium nitrate, and ammonium acetate; urea; aqueous ammonia; sodium nitrate; and potassium nitrate. Nitrogen-containing organic compounds, such as corn steep liquor, meat extract, peptone, N—Z-amine, protein hydrolysate, amino acid, etc. may also be used. These nitrogen sources may be used alone or as a mixture of two or more thereof. The concentration of these nitrogen sources in the culture medium varies depending on the kind of the nitrogen compound, but is usually about 0.1 to 10 w/v %. Examples of the inorganic salts include potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium sulfate, sodium chloride, iron(II) nitrate, manganese sulfate, zinc sulfate, cobalt sulfate, and calcium carbonate. These inorganic salts may be used alone or as a mixture of two or more thereof. The concentration of the inorganic salts in the culture medium varies depending on the kind of the inorganic salts, but is usually about 0.01 to 1 w/v %. Examples of the nutritional substances include meat extract, peptone, polypeptone, yeast extract, dry yeast, corn steep liquor, skim milk powder, defatted soybean hydrochloric acid hydrolysate, and extract from animals, plants or microorganisms, and degradation products thereof. The concentration of the nutritional substances in the culture medium varies depending on the kind of the nutritional substances, but is usually about 0.1 to 10 w/v %. Further, vitamins may be added as needed. Examples of the vitamins include biotin, thiamine (vitamin B1), pyridoxine (vitamin B6), pantothenic acid, inositol, nicotinic acid, etc. The pH of the culture medium is preferably about 6 to 8. Specific examples of the preferable culture medium for coryneform bacteria include A medium (Inui, M. et al., Metabolic analysis of As the reaction mixture, water, a buffer solution, an inorganic salt medium, or the like, containing a phenol precursor (raw material for phenol) can be used. As the precursor, tyrosine (L-tyrosine, D-tyrosine, or a mixture thereof), a salt thereof, or an ester thereof may be used. Inter alia, preferred is L-tyrosine, a salt thereof, or an ester thereof. Examples of the salt include a sodium salt, a potassium salt, and a hydrochloride. Examples of the ester include esters with alcohols having 1 to 4 carbon atoms. Since tyrosine is poorly soluble in water, preferably used is a tyrosine salt, and more preferred is a sodium salt. These precursors may be used alone or a mixture of two or more kinds. The concentration of tyrosine, a salt thereof, or an ester thereof in the reaction mixture is preferably about 0.5 to 10 w/v %, more preferably about 1 to 7 w/v %, and still more preferably about 2 to 5 w/v %. When the concentration is in the above range, phenol can be efficiently produced. Examples of the buffer solution include a phosphate buffer, a Tris buffer, a carbonate buffer, etc. The concentration of the buffer solution is preferably about 10 to 150 mM. Examples of the inorganic salt medium include a medium containing one or more kinds of inorganic salts including potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium sulfate, sodium chloride, iron(II) nitrate, manganese sulfate, zinc sulfate, cobalt sulfate, and calcium carbonate. Inter alia, preferred is a medium containing magnesium sulfate. Specific example of the inorganic salt medium include BT medium (Omumasaba, C. A. et al., The pH of the reaction mixture is preferably about 6 to 8. During the reaction, the pH of the reaction mixture is preferably kept nearly neutral, in particular at around 7 with the use of aqueous ammonia, aqueous sodium hydroxide, or the like, under the control of a pH controller (for example, Type: DT-1023 made by Able). The reaction temperature, that is, the temperature for keeping the transformant alive during the reaction is preferably about 20 to 50° C., and more preferably about 25 to 47° C. When the temperature is in the above range, phenol can be efficiently produced. The reaction period is preferably about 1 to 7 days, and more preferably about 1 to 3 days. The culture may be a batch process, a fed-batch process, or a continuous process. Inter alia, a batch process is preferred. The reaction may be performed under aerobic conditions or reducing conditions, but preferably is performed under reducing conditions. Under reducing conditions, coryneform bacteria do not substantially proliferate and can further efficiently produce phenol. The “reducing conditions” is defined based on the oxidation-reduction potential of the reaction mixture. The oxidation-reduction potential of the reaction mixture is preferably about −200 mV to −500 mV, and more preferably about −250 mV to −500 mV. The reducing conditions of the reaction mixture can be simply estimated with the use of resazurin indicator (in reducing conditions, decolorization from blue to colorless is observed). However, for precise measurement, a redox-potential meter (for example, ORP Electrodes made by BROADLEY JAMES) is used. As a method of preparing a reaction mixture under reducing conditions, any publicly known method can be used without limitation. For example, as a liquid medium for preparation of the reaction mixture, an aqueous solution for a reaction mixture may be used instead of distillated water or the like. As reference for preparation of the aqueous solution for a reaction mixture, for example, the method for preparing a culture medium for strictly anaerobic microorganisms, such as sulfate-reducing microorganisms (Pfennig, N. et al.: The dissimilatory sulfate-reducing bacteria, In The Prokaryotes, A Handbook on Habitats, Isolation and Identification of Bacteria, Ed. by Starr, M. P. et al. Berlin, Springer Verlag, 926-940, 1981, or Specifically, by treating distillated water or the like with heat or under reduced pressure for removal of dissolved gases, an aqueous solution for a reaction mixture under reducing conditions can be obtained. In this case, for removal of dissolved gases, especially dissolved oxygen, distillated water or the like may be treated under reduced pressure of about 10 mmHg or less, preferably about 5 mmHg or less, more preferably about 3 mmHg or less, for about 1 to 60 minutes, preferably for about 5 to 40 minutes. Alternatively, by adding a suitable reducing agent (for example, thioglycolic acid, ascorbic acid, cysteine hydrochloride, mercaptoacetic acid, thiol acetic acid, glutathione, sodium sulfide, etc.), an aqueous solution for a reaction mixture under reducing conditions can be prepared. These methods may be suitably combined to prepare an effective aqueous solution for a reaction mixture under reducing conditions. It is preferred to maintain the reducing conditions of the reaction mixture during the reaction. For maintenance of reducing conditions, it is preferred that oxygen from the outside of the reaction system is prevented to the utmost extent from entering the system. Specific examples of the method employed for this purpose include a method comprising encapsulating the reaction system with inert gas, such as nitrogen gas, carbon dioxide gas, etc. In some cases, for allowing the metabolic functions in the cells of the aerobic bacterium of the present invention to work effectively during the reaction, addition of a solution of various nutrients or a reagent solution for adjusting and maintaining the pH of the reaction system may be needed. In such a case, for more effective prevention of oxygen incorporation, it is effective to remove oxygen in the solutions to be added, in advance. Through the culture performed in the above manner, phenol is produced in the reaction mixture. Phenol can be collected by collecting the reaction mixture, and it is also feasible to isolate phenol from the reaction mixture by a known method. Examples of such a known method include distillation, the membrane permeation method, and the organic solvent extraction method. Hereinafter, the present invention will be described in more detail by way of Examples, but the present invention is not limited thereto. (1) Extraction of Chromosomal DNA from Microorganisms To extract chromosomal DNA from To extract chromosomal DNA from Construction of Cloning Vector pCRB22 A DNA fragment comprising a DNA replication origin sequence of pCASE1, a plasmid derived from In the PCR, the following sets of primers were synthesized based on SEQ ID NO: 1 (pCASE1-ori sequence) and SEQ ID NO: 2 (cloning vector pHSG298) for cloning of the pCASE1-ori sequence and the cloning vector pHSG298, and were used. Primers for pCASE1-ori sequence amplification Primers (a-1) and (b-1) each have a BglII restriction enzyme site added thereto. Primers for cloning vector pHSG298 amplification Primers (a-2) and (b-2) each have a BglII restriction enzyme site added thereto. As the template DNA, total DNA extracted from Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara Bio, Inc.) as a reaction reagent under the conditions described below. Denaturation step: 94° C., 60 seconds Annealing step: 52° C., 60 seconds Extension step: 72° C.
A cycle consisting of the above 3 steps was repeated 30 times. Using 10 μL of the above-produced reaction mixture, 0.8% agarose gel electrophoresis was performed. In the case of the pCASE1-ori sequence, an about 1.4-kb DNA fragment was detected. In the case of the cloning vector pHSG298, an about 2.7-kb DNA fragment was detected. 10 μL of the about 1.4-kb DNA fragment comprising the pCASE1-ori sequence derived from With the use of the Ligation Liquid A, A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of restriction enzyme BglII to confirm the inserted fragment. As a result, in addition to an about 2.7-kb DNA fragment of the cloning vector pHSG298, an about 1.4-kb DNA fragment of the pCASE-ori sequence was confirmed. The cloning vector comprising the pCASE1-ori sequence was named pCRB22. Construction of Cloning Vector pCRB207 A DNA fragment comprising a promoter sequence of the gapA gene encoding the glyceraldehyde-3-phosphate dehydrogenase (hereinafter abbreviated as PgapA) derived from In the PCR, the following sets of primers were synthesized based on SEQ ID NO: 7 (PgapA sequence) and SEQ ID NO: 8 (terminator sequence) for cloning of the PgapA sequence and the terminator sequence, and were used. Primer (a-3) has a SalI restriction enzyme site added thereto, and primer (b-3) has SalI, BamHI, and NcoI restriction enzyme sites added thereto. Primer (a-4) has SphI and NcoI restriction enzyme sites added thereto, and primer (b-4) has SphI and BspHI restriction enzyme sites added thereto. As the template DNA, the chromosomal DNA extracted from Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara Bio, Inc.) as a reaction reagent under the conditions described below. Denaturation step: 94° C., 60 seconds Annealing step: 52° C., 60 seconds Extension step: 72° C.
A cycle consisting of the above 3 steps was repeated 30 times. Using 10 μL of the above-produced reaction mixture, 0.8% agarose gel electrophoresis was performed. In the case of the PgapA sequence, an about 0.6-kb DNA fragment was detected. In the case of the terminator sequence, an about 0.4-kb DNA fragment was detected. 10 μL of the about 0.6-kb DNA fragment comprising the PgapA sequence derived from With the use of the Ligation Liquid B, A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of restriction enzyme SalI to confirm the inserted fragment. As a result, in addition to an about 4.1-kb DNA fragment of the cloning vector pCRB22, an about 0.6-kb DNA fragment of the PgapA sequence was confirmed. The cloning vector comprising the PgapA sequence was named pCRB206. 10 μL of the about 0.4-kb DNA fragment comprising the terminator sequence derived from the plasmid pKK223-3, which was amplified by the above PCR, was cut with the use of restriction enzymes NcoI and BspHI, 2 μL of the above cloning vector pCRB206 was cut with the use of restriction enzyme NcoI, and both were processed at 70° C. for 10 minutes for deactivation of the restriction enzymes. Both were mixed, and 1 μL of T4 DNA ligase 10× buffer solution and 1 unit of T4 DNA ligase (made by Takara Bio, Inc.) were added thereto. Sterile distilled water was added thereto so that the total volume was 10 μL, and the mixture was allowed to react at 15° C. for 3 hours for ligation. This was named Ligation Liquid C. With the use of the Ligation Liquid C, A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of the restriction enzyme to confirm the inserted fragment. As a result, in addition to an about 4.7-kb DNA fragment of the cloning vector pCRB206, an about 0.4-kb DNA fragment of the terminator sequence was confirmed. The cloning vector comprising the rrnBT1T2 terminator sequence was named pCRB207. Construction of Cloning Vector pCRB209 A DNA fragment comprising a promoter sequence of the gapA (glyceraldehyde 3-phosphate dehydrogenase A) gene (hereinafter abbreviated as PgapA) derived from In the PCR, the following set of primers was synthesized based on SEQ ID NO: 13 (pCRB207) for cloning of the pCRB207 sequence, and was used. Primers for pCRB207 Sequence Amplification Primers (a-5) and (b-5) each have an NdeI restriction enzyme site added thereto. As the template DNA, the cloning vector pCRB207 comprising a gapA promoter and a rrnBT1T2 terminator sequence was used. Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara SHUZO) as a reaction reagent under the conditions described below. Denaturation step: 94° C., 60 seconds Annealing step: 52° C., 60 seconds Extension step: 72° C., 307 seconds A cycle consisting of the above 3 steps was repeated 30 times. Using 10 μL of the above-produced reaction mixture, 0.8% agarose gel electrophoresis was performed, and an about 5.1-kb DNA fragment comprising the cloning vector pCRB207 was detected. 10 μL of the about 5.1-kb DNA fragment comprising the gene derived from pCRB207, which was amplified by the above PCR, was cut with the use of restriction enzyme NdeI and processed at 70° C. for 10 minutes for deactivation of the restriction enzyme. To this, 1 μL of T4 DNA ligase 10× buffer solution and 1 unit of T4 DNA ligase (made by Takara SHUZO) were added. Sterile distilled water was added thereto so that the total volume was 10 μL, and the mixture was allowed to react at 15° C. for 3 hours for ligation. This was named Ligation Liquid D. With the use of the Ligation Liquid D, A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of restriction enzyme NdeI to confirm the inserted restriction enzyme site. The cloning vector comprising the PgapA sequence and the rrnBT1T2 terminator sequence was named pCRB209. Cloning of Phenol-Producing Gene Derived from A DNA fragment comprising the tpl gene which is derived from In the PCR, the following set of primers was synthesized based on SEQ ID NO: 16 (the tpl gene of Primers (a-6) and (b-6) each have an NdeI restriction enzyme site added thereto. As the template DNA for Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara Bio, Inc.) as a reaction reagent under the conditions described below. Denaturation step: 94° C., 60 seconds
A cycle consisting of the above 3 steps was repeated 30 times. With the use of 10 μl of the reaction mixture produced above, 0.8% agarose gel electrophoresis was performed. As a result, detected was an about 1.4-kb DNA fragment of the Cloning of Phenol-Producing Gene to pCRB209 10 μL of the about 1.4-kb DNA fragment comprising the tpl gene derived from With the use of the obtained Ligation Liquid E, A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of restriction enzyme to confirm the inserted fragment. As a result, in addition to an about 5.1-kb DNA fragment of the plasmid pCRB209, confirmed was an about 1.4-kb inserted fragment of the tpl gene derived from The plasmid comprising the tpl gene derived from (5) Construction of Plasmid for A DNA fragment required for constructing a plasmid for markerless disruption of the poxF gene on the chromosome of In the PCR, the following sets of primers were synthesized based on the sequence of Primers for Amplification of poxF-1 Region Primer (a-7) has an XbaI restriction enzyme site added thereto. Primers for Amplification of poxF-2 Region Primer (b-8) has an XbaI restriction enzyme site added thereto. As the template DNA, the chromosomal DNA extracted from Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara Bio, Inc.) as a reaction reagent under the conditions described below. Denaturation step: 94° C., 60 seconds Annealing step: 52° C., 60 seconds Extension step: 72° C.
A cycle consisting of the above 3 steps was repeated 30 times. Using 10 μL of the above-produced reaction mixture, 0.8% agarose gel electrophoresis was performed. An about 0.8-kb DNA fragment in the case of the Subsequently, 1 μL each of the poxF-1 region fragment and the poxF-2 region fragment, which were amplified by the above PCR, were mixed and subjected to PCR for ligation. Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara Bio, Inc.) as a reaction reagent under the conditions described below. Denaturation step: 95° C., 20 seconds Annealing step: 52° C., 5 seconds Extension step: 72° C., 50 seconds A cycle consisting of the above 3 steps was repeated 30 times. Further, using, as the template DNA, the obtained fragment in which poxF-1 and poxF-2 were ligated, a poxF deletion fragment was amplified by PCR. Actual PCR was performed with the use of a thermal cycler, GeneAmp PCR System 9700 (made by Applied Biosystems) and TaKaRa LA Taq (made by Takara Bio, Inc.) as a reaction reagent under the conditions described below. Denaturation step: 95° C., 20 seconds Annealing step: 52° C., 5 seconds Extension step: 72° C., 50 seconds A cycle consisting of the above 3 steps was repeated 30 times. Using 10 μL of the above-produced reaction mixture, 0.8% agarose gel electrophoresis was performed, and an about 1.6-kb fragment of the poxF deletion fragment was detected. 10 μL of the about 1.7-kb DNA fragment of the poxF deletion fragment derived from With the use of the Ligation Liquid F, A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of restriction enzyme XbaI to confirm the inserted fragment. As a result, in addition to an about 4.4-kb DNA fragment of the plasmid pCRA725, an about 1.7-kb inserted fragment of the poxF deletion gene derived from The plasmid comprising the poxF deletion gene derived from (6) Construction of Strain in which a Gene Associated with Degradation of Phenol is Disrupted Vector pCRA725 for markerless chromosomal gene transfection is a plasmid that cannot be replicated within In the case of a strain having a single crossover of the plasmid pCRA725-poxF/CG with the homologous region on the chromosome, the strain shows kanamycin resistance resulting from the expression of the kanamycin resistance gene on the pCRA725-poxF/CG and mortality on a culture medium containing sucrose resulting from the expression of the The obtained markerless poxF gene disruptant of With the use of the above-described plasmid pCRB209-tpl/PA, transformation of A growing strain on the culture medium was subjected to liquid culture in the usual manner. Plasmid DNA was extracted from the culture and cut with the use of restriction enzyme to confirm the inserted plasmid. As a result, transfection of the above-constructed plasmid pCRB209-tpl/PA was confirmed. The obtained strain was named The An inoculation loop of the The The bacterial cells cultured and proliferated as above were collected by centrifugation (5,000×g at 4° C. for 15 minutes). The obtained bacterial cells were suspended in 50 mL of BT (-urea) liquid medium (0.7% ammonium sulfate, 0.05% potassium dihydrogen phosphate, 0.05% dipotassium hydrogen phosphate, 0.05% magnesium sulfate heptahydrate, 0.0006% iron sulfate heptahydrate, 0.00042% manganese sulfate hydrate, 0.00002% biotin and 0.00002% thiamine hydrochloride) so that the final concentration of the bacterial cell was 10%. To a 100-mL medium bottle, the cell suspension was transferred, L-tyrosine disodium salt was added as a substrate, and the reaction was allowed to proceed under reducing conditions (the ORP of the reaction mixture: −450 mV) in a water bath kept at 33° C. with stirring. As for the addition of L-tyrosine disodium salt, 40 mM L-tyrosine disodium salt was added at 0, 1, 3, and 10 hours after the start of the reaction. A sample of the reaction mixture was centrifuged (15,000×g at 4° C. for 10 minutes), and the obtained supernatant was used for quantitative determination of phenol. As a result, in the reaction under reducing conditions, A growth inhibition test in aerobic culture was performed to examine the influence of phenol on An inoculation loop of the The An inoculation loop of the The An inoculation loop of each of the The The proliferation of In contrast, the proliferation of Thus, it was shown that According to the process of the present invention, phenol can be produced from tyrosine with a practical efficiency using microorganisms. Provided is a phenol-producing transformant constructed by transferring a gene which encodes an enzyme having tyrosine phenol-lyase activity into a coryneform bacterium as a host. Also provided is a process for producing phenol, which comprises a step of allowing the transformant to react in a reaction mixture containing tyrosine, a salt thereof, or an ester thereof under reducing conditions, and a step of collecting phenol from the reaction mixture. 1. A phenol-producing transformant constructed by transferring a gene which encodes an enzyme having tyrosine phenol-lyase activity into a coryneform bacterium as a host. 2. The transformant of 3. The transformant of (a) a DNA consisting of the base sequence of SEQ ID NO: 16, a DNA consisting of the base sequence of SEQ ID NO: 23, a DNA consisting of the base sequence of SEQ ID NO: 24, a DNA consisting of the base sequence of SEQ ID NO: 25, a DNA consisting of the base sequence of SEQ ID NO: 26, or a DNA consisting of the base sequence of SEQ ID NO: 27 (b) a DNA which hybridizes to a DNA consisting of a complementary base sequence of any of the DNAs of (a) under stringent conditions and which encodes a polypeptide having tyrosine phenol-lyase activity 4. The transformant of 5. The transformant of 6. The transformant of 7. The transformant of 8. A 9. A process for producing phenol, which comprises a step of allowing the transformant of 10. The process of 11. The process of TECHNICAL FIELD
BACKGROUND ART
CITATION LIST
Patent Literature
SUMMARY OF INVENTION
Technical Problem
Solution to Problem
(ii) The transformant can further efficiently produce phenol in the case where the phenol 2-monooxygenase gene (poxF) on the chromosome of the coryneform bacterium as the host has a disruption or deletion.
(iii) The transformant has a particularly higher phenol productivity when proliferation is substantially inhibited in a reaction mixture under reducing conditions.
[2] The transformant of the above, wherein the gene which encodes an enzyme having tyrosine phenol-lyase activity is a gene derived from
[3] The transformant of the above, wherein the gene which encodes an enzyme having tyrosine phenol-lyase activity is the DNA of the following (a) or (b).
(a) a DNA consisting of the base sequence of SEQ ID NO: 16, a DNA consisting of the base sequence of SEQ ID NO: 23, a DNA consisting of the base sequence of SEQ ID NO: 24, a DNA consisting of the base sequence of SEQ ID NO: 25, a DNA consisting of the base sequence of SEQ ID NO: 26, or a DNA consisting of the base sequence of SEQ ID NO: 27
(b) a DNA which hybridizes to a DNA consisting of a complementary base sequence of any of the DNAs of (a) under stringent conditions and which encodes a polypeptide having tyrosine phenol-lyase activity
[4] The transformant of any one of the above to, wherein the coryneform bacterium as the host is a coryneform bacterium in which a gene which encodes an enzyme having phenol 2-monooxygenase activity on the chromosome is disrupted or deleted.
[5] The transformant of any one of the above to, wherein the coryneform bacterium as the host is
[6] The transformant of any one of the above to, wherein the coryneform bacterium as the host is
[7] The transformant of any one of the above to, wherein the coryneform bacterium as the host is a strain of
[8] A
[9] A process for producing phenol, which comprises a step of allowing the transformant of any one of the above to to react in a reaction mixture containing tyrosine, a salt thereof, or an ester thereof under reducing conditions, and a step of collecting phenol from the reaction mixture.
[10] The process of the above, wherein the transformant does not substantially proliferate in the reaction step.
[11] The process of the above or, wherein the oxidation-reduction potential of the reaction mixture under reducing conditions is −200 mV to −500 mV.
Advantageous Effects of Invention
BRIEF DESCRIPTION OF DRAWINGS
DESCRIPTION OF EMBODIMENTS
(I) Phenol-Producing Transformant
Host
Construction of Vector for Transformation
Transformation
Disruption or Deletion in Host Chromosomal Gene
(II) Process for Producing Phenol
Proliferation of Microorganism
Culture Medium
Reaction Mixture
Reaction Conditions
<Reducing Conditions>
Collection of Phenol
EXAMPLES
Example 1
Cloning and Expression of Phenol-Producing Gene
(2) Construction of Cloning Vectors
(SEQ ID NO: 3) (a-1); 5′-AT AGATCT AGAACGTCCGTAGGAGC-3′ (SEQ ID NO: 4) (b-1); 5′-AT AGATCT GACTTGGTTACGATGGAC-3′ (SEQ ID NO: 5) (a-2): 5′-AT AGATCT AGGTTTCCCGACTGGAAAG-3′ (SEQ ID NO: 6) (b-2): 5′-AT AGATCT CGTGCCAGCTGCATTAATGA-3′ Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL Template DNA 5 μL (DNA content: 1 μg or less) The above 2 primers*) 0.5 μL each (final conc.: 1 μM) Sterile distilled water 25.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)For amplification of the pCASE1-ori sequence, a combination of primers (a-1) and (b-1), and for amplification of the cloning vector pHSG298, a combination of primers (a-2) and (b-2) were used. PCR Cycle:
Primers for PgapA Sequence Amplification
(SEQ ID NO: 9) (a-3); 5′-CTCT GTCGAC CCGAAGATCTGAAGATTCCTG-3′ (SEQ ID NO: 10) (b-3); 5′-CTCT GTCGACGGATCCCCATGG TGTGTCTCCTCTAAAGATTGTAGG-3′ Primers for Terminator Sequence Amplification
(SEQ ID NO: 11) (a-4); 5′-CTCT GCATGCCCATGG CTGTTTTGGCGGATGAGAGA-3′ (SEQ ID NO: 12) (b-4); 5′-CTCT GCATGCTCATGA AAGAGTTTGTAGAAACGCAAAAAGG-3′ Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL Template DNA 5 μL (DNA content: 1 μg or less) The above 2 primers*) 0.5 μL each (final conc.: 1 μM) Sterile distilled water 25.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)For amplification of the PgapA sequence, a combination of primers (a-3) and (b-3), and for amplification of the terminator sequence, a combination of primers (a-4) and (b-4) were used. PCR Cycle:
(SEQ ID NO: 14) (a-5); 5′-CTCT CATATG CTGTTTTGGCGGATGAGAG-3′ (SEQ ID NO: 15) (b-5); 5′-CTCT CATATG GTGTCTCCTCTAAAGATTGTAGG-3′ Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL Template DNA 5 μL (DNA content: 1 μg or less) The above 2 primers*) 0.5 μL each (final conc.: 1 μM) Sterile distilled water 25.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)For amplification of the pCRB207 sequence, a combination of primers (a-5) and (b-5) was used. PCR Cycle:
(3) Cloning of Phenol-Producing Gene
Primers for tpl Gene Amplification
(SEQ ID NO: 17) (a-6); 5′-CTCT CATATG AACTATCCTGCCGAGC-3′ (SEQ ID NO: 18) (b-6); 5′-CTCT CATATG TTAAATAAAGTCAAAACGCGCAGTAAAG-3′ Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL Template DNA 5 μL (DNA content: 1 μg or less) The above 2 primers*) 0.5 μL each (final conc.: 1 μM) Sterile distilled water 25.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)For amplification of the tpl gene of PCR Cycle:
Annealing step: 52° C., 60 seconds
Extension step: 72° C.
(4) Construction of Phenol-Producing Gene Expression Plasmid
Construction of Plasmid for (SEQ ID NO: 19) (a-7); 5′-CTCT TCTAGA TACGTCCTAAACACCCGAC-3′ (SEQ ID NO: 20) (b-7); 5′-GACCAACCATTGCTGACTTGCGTATCCATAGTCAGGCTTC-3′ (SEQ ID NO: 21) (a-8); 5′-CAAGTCAGCAATGGTTGGTC-3′ (SEQ ID NO: 22) (b-8); 5′-CTCT TCTAGA TGATCAGTACCAAGGGTGAG-3′ Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL Template DNA 5 μL (DNA content: 1 μg or less) The above 2 primers*) 0.5 μL each (final conc.: 1 μM) Sterile distilled water 25.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)For amplification of the poxF-1 region, a combination of primers (a-7) and (b-7), and for amplification of the poxF-2 region, a combination of primers (a-8) and (b-8) were used. PCR Cycle:
Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL The above 2 fragments*) 1 μL each Sterile distilled water 29.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)poxF-1 region fragment and poxF-2 region fragment were used. PCR Cycle:
Reaction Mixture:
TaKaRa LA Taq ™ (5 units/μL) 0.5 μL 10X LA PCR ™ Buffer II 5 μL (Mg2+ free) 25 mM MgCl2 5 μL dNTP Mixture (2.5 mM each) 8 μL Template DNA 5 μL (DNA content: 1 μg or less) The above 2 primers*) 0.5 μL each (final conc.: 1 μM) Sterile distilled water 25.5 μL The above ingredients were mixed, and 50 μL of the reaction mixture was subjected to PCR. *)For amplification of the poxF deletion fragment, a combination of primers (a-7) and (b-8) was used. PCR Cycle:
(7) Construction of Transgenic Strain for Phenol-Producing Gene
Example 2
Experiment of Phenol Production Using
Example 3
Test for Suitability as a Host for Phenol Production
Influence of Phenol on Aerobic Proliferation
INDUSTRIAL APPLICABILITY
