MICROORGANISM HAVING ENHANCED PRODUCTIVITY OF LACTIC ACID AND A PROCESS FOR PRODUCING LACTIC ACID USING THE SAME
The present invention relates to a lactic acid-producing recombinant Generally, lactic acid is an important organic acid with a wide range of applications including food additives such as food preservative, fragrance, or acidifier etc., and has been used broadly for industrial purposes such as cosmetics, chemistry, metals, electronics, fabrics, dyeing textiles, and pharmaceutical industries, etc. In addition, lactic acid is an essential ingredient of polylactic acid, one of biodegradable plastics, and thus the demand for lactic acid has been increasing significantly. It is also used as an important material for the productions of many chemical compounds including polylactic acid, acetaldehyde, polypropylene glycol, acrylic acid, 2,3-pentathione, etc. Specifically, D-type lactic acid is an essential ingredient for producing streocomplex PLA, which is an optical isomer required for the production of highly heat-resistant PLA. Specifically, the method for producing lactic acid includes a traditional chemical synthesis and a biological fermentation process. When lactic acid is produced via the chemical synthesis, lactic acid is produced in the form of a racemic, mixture consisting of 50% D-type lactic acid and 50% L-type lactic acid, and it difficult to control the composition ratio, and thus polylactic acid produced therefrom may become an amorphous polymer having a low melting point, thereby imposing limitations on the development of their use. On the other hand, the biological fermentation process allows to selectively produce D-type lactic acid or L-type lactic acid depending on the strain used. Thus, the latter is preferred commercially because it is possible to produce a particular isoform of lactic acid. Meanwhile, attempts have been made in order to improve the productivity of lactic acid via various gene manipulations using a Accordingly, intensive efforts have been made by the present inventors in order to obtain a microorganism having improved lactic acid productivity with an efficient cell growth while decreasing the activity of PDC. As a result, it has been confirmed that strains, in which the activities of PDC isotypes were controlled and the activities of aldehyde dehydrogenase and acetyl-CoA were increased, were able to increase the lactic acid production yield and facilitate the cell growth of the strains, thereby improving the overall lactic acid fermentation productivity, and this has led to the completion of the present invention. An objective of the present invention is to provide a Another objective of the present invention is to provide a method for producing lactic acid using the In a first aspect of the present invention, to achieve the objectives described above, there is provided a Generally, a lactic acid-producing The tetra “pyruvate decarboxylase (PDC) used herein refers to a protein having an activity capable of mediating a reaction responsible for producing carbonic acid and acetaldehyde from pyruvate, but is not limited to any derivative thereof or an isotype having the same activity. The protein has been known to be involved in a step of alcohol fermentation, and is mostly present in yeasts and plants. The pyruvate decarboxylase of the present invention may be intrinsically present in a The term “homology” used herein refers to a degree of similarity between a plurality of nucleotide sequences or amino acid sequences, and is a unit representing a sequence having the same sequences to the amino acid sequences or the nucleotide sequences of the present invention, with a probability equal to or greater than the above probability. Such homology may be determined by comparing the two given sequences with the naked eye, but rather, it may be measured using a sequence comparison program, which is easily accessible, that interprets the degree of homology by arranging the sequences to be compared side by side. The sequence comparison programs known in the art include FASTP, BLAST, BLAST2, PSIBLAST, and a software containing CLUSTAL W, etc. Numerous examples have been reported regarding the production of lactic acid by allowing a defect in PDC1, whose exhibits a major activity in lactic acid production (Appl Microbiol Biotechnol. 2009, 82(5):883-90). In this case, since PDC6 is rarely expressed, the actual PDC activity as appears to be due to the expression of PDC5 gene. According to the reports, the defectin PDC1 alone does not hinder the cell growth of a wild-type strain, and also about 60-70% of PDC activity can be maintained compared to that of the wild-type, and thus no significant phenotypic change has been observed in the strain (J Bacteriol, 1990, 172(2):678-685). As an alternative, a strain having a simultaneous double defect in both PDC1 and PDC5 genes, which exhibit major PDC activities in yeasts, may be prepared. In such case, lactic acid fermentation can be carried out using a sugar source such as glycogen in the absence of a co-substrate such as acetic acid or ethanol. However, it resulted in decrease in the growth rate of the yeast strain due to a rapid decrease in PDC activity, thereby reducing the fermentation productivity of lactic acid (Biosci Biotechnol Biochem. 2006, 70(5):1148-1153). Meanwhile, in order to maximize the lactic acid via LDH pathway, which competes with PDC for pyruvate, a strain with a simultaneous triple defect in PDC1, PDC5, and PDC6 may be prepared. In this case, lactic acid fermentation yield may be maximized but the metabolic capabilities of ethanol and acetic acid due to catabolite repression induced in the presence of glucose may be further inhibited, thereby reducing cell growth and ultimately leading to decrease in fermentation productivity (Curr Genet. 2003, 43(3): 139-160). Specifically, the decrease in pyruvate decarboxiyase (PDC) activity of the present invention may i) inactivate PDC1 activity and decrease PDC5 activity; or ii) decrease PDC1 activity and inactivate PDC 5 activity. In an exemplary embodiment of the present invention, four different strains, which include a strain with a decreased PDC5 activity by substituting the promoter of PDC5 gene, a strain that caused a defect in PDC5 gene t by recovering PDC1 activity, a strain that caused a double defect in PDC1 and PDC5 genes, and a strain that caused a triple defect in PDC1, PDC5, and PDC6 genes, were prepared based on a The term “aldehyde dehydrogenase (ALD)” used herein refers to a protein having an activity of mainly producing acetic acid from acetaldehyde as a protein having an activity of producing carboxylic acid or an acyl group by the oxidation of aldehyde, but is not limited to a derivative thereof or an isotype having the same activity, in the present invention. The aldehyde dehydrogenase of the present invention may be derived from a The term “acetyl-CoA synthetase (ACS) used herein refers to a protein having an activity of catalyzing the thioesterification of acetic acid and CoA in conjugation with an ATP decomposition reaction, but is not limited to a derivative or an isotype having the same activity in the present invention. It has been known that the protein is present in microorganisms, plants, and animals, etc. The acetyl-CoA synthetase of the present invention may be derived from a In an exemplary embodiment of the present invention, strains, in which the activities of ALD2 and ACS, or the activities of ALD3 and ACS were increased, were prepared based on the strain having a decreased PDC activity compared to that of a non-mutated microorganism, Specifically, strains having increased activities of ALD and ACS were prepared based on the strain having inactivated PDC1 via PDC1 defect and decreased PDC5 activity by substituting the gene promoter of PDC5 with a promoter having low expression ability. More specifically, strains of The term “inactivation” of an enzyme activity of the present invention refers to a method for inactivating enzyme activities including; any method that inhibits the expression of an enzyme, or allows the expression of an enzyme incapable of exhibiting its original activities. The method may include a partial gene deletion or a whole gene deletion caused by a homology recombination, an inhibition of an enzyme expression caused by an insertion of a foreign-derived gene into the relevant gene, an inhibition of an enzyme expression caused by a substitution or modification of a gene promoter sequence of the enzyme, or a mutation into an inactive-enzyme having a loss in its original functions caused by a substitution or modification of the enzyme, etc., but is not limited thereto. The term “decrease” of an enzyme activity used herein refers to a method for decreasing the activity of an enzyme including any method for decreasing the expression level of an enzyme, or decreasing the activity of an enzyme being expressed. The method may include a decrease in an expression caused by a substitutionor modification of a promoter sequence of the enzyme gene, or a mutation into an enzyme having decreased activity caused by a substitution or modification of the enzyme, etc., but is not limited thereto. The term “increase” of an enzyme activity used herein refers to insertion of a plasmid containing the genes of an enzyme, an increase in the number of gene copies encoding an enzyme on a chromosome, or an increase in an enzyme activity caused by a substitution or modification, or a imitation of a promoter sequence of an enzyme gene, etc., but is not limited thereto. The term “yeast microorganism” used herein refers to a microorganism belonging to By preparing the microorganism having a decreased activity of PDC and improved activities of ALD and ACS based on The microorganism of the present invention may include alcohol dehydrogenase (ADH) that is to be further inactivated. The term “alcohol dehydrogenase” used herein refers to a protein having an activity of catalyzing a reverse reaction responsible for producing aldehyde or ketone by removing hydrogen from alcohol, but is not limited to a derivative or an isotype having the same activity. Alcohol dehydrogenase of the present invention may be derived from The microorganism of the present invention may include D-lactic acid dehyrogenase (DLD) that is further inactivated. The term “D-lactic acid dehydrogenase” used herein, refers to a protein having an activity of producing pyruvate by anhydrization of D-lactic acid, but is not limited to an isotype having the same activity. D-lactic acid dehydrogenase of the present invention may be derived from In the present invention, the strains having a defect in ADH1, an enzyme involved in alcohol fermentation pathway using aldehyde as a substrate, which is further produced from pyruvate, and a defect in DLD1, an enzyme that decomposes the produced lactic acid, were used to precisely measure the changes in the lactic acid fermentation cell performances according to the regulation of acetic acid production pathway. In an exemplary embodiment of the present invention, the strains, in which the activities of PDC, ALD, and ACS were regulated, showed a significant increase in the lactic acid fermentation productivity. The results are summarized in Table 12. In another aspect, the present invention provides a method for producing lactic acid using the microorganism of the present invention. Specifically, in an exemplary embodiment of the present invention, the present invention provides a method for producing lactic acid including culturing the microorganism of the present invention and collecting lactic acid from the culture medium containing the microorganism. The culturing may be performed using an appropriate medium and culturing conditions known in the art. According to the strains used, the culturing process may be readily adjusted by one of ordinary skill in the art. Examples of culturing methods include batch type,continuous type, and fed-batch type, but are not limited thereto. The media used in the culturing process should appropriately meet the requirements of a specific strain. The medium used in the present invention contains sucrose or glucose as a main carbon source, and molasses containing a high concentration of sucrose may also be used as a carbon source. Other carbon sources may be used in an adequate amount variously. Organic nitrogen sources including peptone, yeast extract, meat extract, malt extract, corn steep liquor, and soybean wheat, and inorganic nitrogen sources including element, ammonium sulfate, ammonium chloride, ammonium phosphate, ammonium carbonate, and ammonium nitrate may be used as a nitrogen source. These nitrogen sources may be employed either singly or in combination. To the medium, phosphorus sources such as potassium dihydrogen phosphate, dipotassium hydrogen phosphate, or corresponding sodium-containing salts may be added. In addition, the medium may contain metal salts such as magnesium sulfate and iron sulfate. Further, the medium may be supplemented with amino acids, vitamins, and appropriate precursors. These media or precursors may be added to cultures by a batch type or continuous type method. During the culturing process, compounds such as ammonium hydroxide, potassium hydroxide, phosphoric acid, and sulfuric acid may be properly added in order to adjust the pH of the culture. Further, a defoaming agent such as fatty acid polyglycol ester may be added in order to inhibit the formation of foams in the culture. In addition, to maintain the culture in an aerobic condition, oxygen or oxygen-containing gas may be injected into the culture, and to maintain the culture in anaerobic and micro-aerobic conditions, nitrogen, hydrogen, or carbon dioxide gases may be injected into the culture without injecting any gas. The temperature of the culture may be maintained at 20 to 40° C., specifically at 25 to 35° C., and more specifically at 30° C. The culturing may be continued until a desired amount of the desired material is obtained, and specifically for 10 to 100 hours. The lactic acid produced in the culturing processes of the present invention may be collected from the culture medium by a proper method known in the art, depending on the culturing method, e.g., batch type, continuous type, or fed-batch type, The present invention relates to using a microorganism having improved lactic acid fermentation productivity by controlling the activities of PDC isotypes, and increasing the activities of aldehyde dehydrogenase (ALM and acetyl-CoA synthetase (ACS). Therefore, it can be extensively used in the lactic acid fermentation production industries. Hereinbelow, the present invention will be described in detail with accompanying exemplary embodiments. However, the exemplary embodiments disclosed herein are only for illustrative purposes and should not be construed as limiting the scope of the present invention. To prepare lactic acid-producing strains, Specifically, a strain, where alcohol dehydrogenase 1 (ADH1) and pyruvate decarboxylase 1 (PDC1) were defective to minimize the loss of pyruvate to the alcohol synthesis pathway, and d-lactic acid dehydrogenase 1 (DLD1) was defective for blocking the D-type lactic acid decomposition pathway, was used as a base strain. DLD1 is not a crucial factor that may have a direct impact on the grow nth improvement, but has been known as a major enzyme capable of converting D-lactic acid to pyruvate using NAD+ as D-lactic acid dehydrogenase. Accordingly, a subsequent strain was constructed based on the strain having gene defects in DLD1, an enzyme that consumes the prepared lactic acid thereof, to compare a complete fermentation productivity of D-type lactic acid-producing yeast, which is intended to be prepared in the present invention. As a result, the fermentation productivity was compared, In the present invention, a general molecular cloning was employed for the gene manipulation. First, in order to delete ADH1 and PDC1 genes of the yeast strains, an experiment was conducted with reference to the content disclosed in the Reference by Lee T H, et al.(J. Microbiol. Biotechnol. (2006), 16(6), 979-982), using plasmids pWAL100 and pWBR100. Each insert, which was introduced into the vector plasmids, was prepared using the suitable primers (corresponding to nucleotide sequences of SEQ ID NOS: I to 8) via PCR. In addition, for the deletion of DLD1 gene, HIS3, which is a marker gene, was introduced by double crossover, and made it defective. The DNA fragments used therein were prepared using primers corresponding to nucleotide sequences of SEQ ID NOS: 9 and 10. The primers used in the gene manipulation are summarized in Table 1 below. D-lactic acid dehydrogenase (D-LDH) specifically required for D-lactic acid production was introduced based on the strain having defects in the three genes such as ADH1, PDC1 and DLD1. D-LDH was then cloned into a vector having restriction enzyme sites of Xhol and Spel at 5′ and 3′ termini, respectively, in order for 1 dhD derived from The construction of pTL573 vector was completed by the ligation of the obtained vector with the insert. The plasmid pTL573 contains the 1 dhD gene derived from A mutant strain having substituted PDC5 promoter was prepared based on CC02-0064 strain prepared in Example 1. During the process, processes of cassette preparation and strain selection were conducted according to the method disclosed in Lee T. H. et at. (Development of reusable split URA3-marked knockout vectors for budding yeast, Specifically, a total of five novel strains were prepared by substituting PDC5 promoter of the CC02-0064 strain with SCO1, SCO2, ACS1, IDP2, and FBA 1 promoters, respectively, and subsequently, promoter-substituted cassettes were prepared using primers corresponding to nucleotide sequences of SEQ ID NOS: 11 to 36. The primers used in the promoter substitution are summarized in Table 2 below. The thus-prepared novel strains were assigned CC02-0167, CC02-0168, CC02-0169, CC02-0170, and CC02-0174, respectively. The corresponding strains and their genetic traits are summarized in Table 3 below. An evaluation of lactic acid fermentation was conducted for the PDCS promoter-mutated strains prepared in Example 2. In this regard, a specific medium was prepared for the evaluation of lactic acid fermentation. Specifically, in order to prepare a synthetic complex media (SC media), a limiting medium for yeast, 0.67% yeast nitrogen base without amino acids serving as a base was mixed with amino acid dropout mix (Sigma) according to the protocol of the manufacturer, and added with the amino acids that were excluded in the base, as needed. In addition, 380 mg/L of leucine was added to the resultant, and uracil, tryptophan, and histidine were added at a concentration of 76 mg/L, respectively. 8% of glucose as a carbon source and 1% of CaCO3as a neutralizing agent were also added. The thus-prepared medium was used for the evaluation of lactic acid fermentation of the yeast strains. Among the PDC5 promoter-mutated strains prepared in Example 2, the mutant strains substituted with a weaker promoter than the original PDC5 promoter failed to grow, whereas the mutant strains substituted with a stronger promoter showed improved growth. Specifically, the mutant strains substituted with promoters of SCO1, SCO2, IDP2 or ACS1, which are weaker promoters than PDC5 promoter, failed to grow, leaving the strains whose promoter was substituted with FBA1 promoter the only strains to be evaluated. The evaluation result of the lactic acid fermentation for CC02-0064 and CC02-0174 strains, which were measurable, is summarized in Table 4 below. As shown in the evaluation above, it was confirmed that, during the pathway promoting acetyl-CoA production, the strain where the wild-type PDC5 promoter was substituted with FBA1 promoter showed improved cell growth rate and lactic acid productivity thereof, compared to those of the original strain (CC02-0064). However, when the result of samples collected at 24 hours and 48 hours, respectively, were compared, it was confirmed that the improvements on the cell growth rate and the lactic acid productivity thereof according to the time were continued to reduce by a mere strengthening of a single PDC activity without strengthening ALD and ACS activities, which are involved in the subsequent acetyl-CoA producing pathway. In an example of the present invention, the improvement in the glucose consumption by the strengthening PDC activity was 10.3%, and the maximum lactic acid production concentration was 47.3 g/l. Accordingly, the overall improvement of the lactic acid productivity was 13.7%. In addition to the strain having a PDC1 gene defect and decreased PDC5 activity prepared in Example 2, a strain having a defect in PDC5 gene and decreased PDC1 activity was prepared to thereby confirm whether PDC pathway was attenuated in the corresponding strain. Specifically, for the purpose of a PDC5 gene defect, the primers corresponding to nucleotide sequences of SEQ ID NOS: 37 to 40 were used to prepare PDC5 gene defect cassette based on the CC02-0064 strain. The defective strain was prepared by the same method described the literature of Example 1. The primers used in Example 4 are summarized in Table 5 below. The thus-prepared strain having a PDC5 gene defect was assigned CC02-0450 (CC02-0064, pdc5Δ). A strain having substituted PDC1 promoter was prepared based on the CC02-0450 strain prepared in Example 4. In this regard, a strain CC02-0451 (CC02-0450, PDC1p-PDC1), where the defect in PDC1 gene was recovered, was prepared to serve as a comparative group, and a strain CC02-0452 (CC02-0450, IDP1p-PDC1) having decreased PDC1 activity was prepared to serve as an experimental group. Each strain was prepared in such a way that the vectors of PDC1p-PDC1-CYC1t and pRS406-IDP2p-PDC1-CYC1, which were constructed by cloning a target gene cassette into a pRS406 vector without a replication origin in the yeast, to be included in the strain. Specifically, PCR was conducted using primers having nucleotide sequences of SEQ ID NOS: 41 and 42 with chromosomal DNA of the yeast serving as a template, to thereby obtain a product including PDC1 gene. Subsequently, a sequence of CYC1 terminator was obtained using primers having nucleotide sequences of SEQ ID NOS: 43 and 44. In addition, DNA fragments connecting PDC1 and CYC1 terminator were obtained via PCR using primers corresponding nucleotide sequences of SEQ ID NOS: 41 and 44 with the PDC1 and the CYC1 terminator sequences, respectively, serving as a template. A plasmid vector of pRS406-PDC1-CYC1t was obtained by treating DNA fragments of PDC1-CYC1 terminator and pRS'406 vector with Spel and Xhol restriction enzymes followed by ligation thereof. Meanwhile, for the introduction of the promoter domain into the thus-obtained plasmid vectors, plasmid vectors, into which promoters of PDC1 and IDP2 promoters were respectively incorporated, were obtained by a primer fusion of primers having nucleotide sequences of SEQ ID NOS: 45 and 46, and 47 and 48, respectively, via PCR using chromosomal DNA as a template. DNA fragments including each promoter and pRS406-PDC1-CYC1t plasmid were digested and ligated, to thereby prepare plasmid vectors of pRS406-PDC1p-PDC1-CYC1t and pRS406-IDP2p-PDC1-CYC1t, respectively, which are plasmid required for the yeast chromosomal insertion, designed such that the gene expression is controlled by PDC1 promoter and IDP2 promoter. The primers used in Example 5 are summarized in Table 6. The two thus-prepared plasmid vectors were digested by StuI, respectively, and inserted into the strains immediately. The final strains were assigned CC02-0451(CC02-0450, PDC 1p-PDC1) and CC02-0452(CC02-0450, IDP2p-PDC1), respectively. The thus-prepared strains and their genetic traits are summarized in Table 7. Strains having a single defect in PDC1 gene, a double defect in PDC1 and PDC5 genes, and a triple defect in PDC1, PDC5, and PDC6 genes were intended to be prepared from PDC family genes. CC02-0064 strain prepared in Example 1 was used as a strain having a single defect in PDC1 gene. A cassette for PDC5 defect was prepared using primers corresponding nucleotide sequences of SEQ ID NOS: 49 to 56, and inserted into CC02-0064 to prepare a strain having double defects in PDC1 and PDC5 genes. Subsequently, the thus-prepared strain was assigned CC02-0256. In addition, a strain having a triple defect in PDC1, PDC5, and PDC6 genes was prepared based on the strain having double defects in PDC1 and PDC5 genes using primers corresponding nucleotide sequence of SEQ ID NOS: 57 to 64 to, and was assigned CC02-0257. The defect cassette preparation and strain selection process were conducted by the same method described in the literature disclosed in Example 1. The primers used in Example 6 are summarized in Table 8. The thus-prepared strains and their genetic traits are summarized in Table 9. For the preparation of ALD and ACS1 over expressing strains, ALD2, ALD3, and ACS1 over expressing plasmids were prepared. Specifically, an open reading frame (ORF) of ALD2 was prepared using primers corresponding nucleotide sequences of SEQ ID NOS: 65 and 66, an ORF of ALD3 was prepared using primers corresponding nucleotide sequences of SEQ ID NOS: 67 and 68, and an ORF of ACS1 was prepared using primers corresponding nucleotide sequences of SEQ ID NOS: 69 and 70. In addition, p415ADH-ALD2, p415ADH-ALD3, p414ADH-ACS1 and p416ADH-ACS1, which are p414ADH, p415ADH and p416ADH plasmid-based recombinant vectors, were prepared by SpeI, Xhol or EcoRI restriction enzymes. The primers used in Example 7 are summarized in Table 10 below. The thus-prepared recombinant plasmids were introduced into the strains including CC02-0064, CC02-0168 CC02-0170 CC02-0256, CC02-0257, CC02-0451, and CC02-0452 via a yeast transformation by p415ADH-ALD2, p414ADH-ACS1 combination, p415ADH-ALD3, p414ADH-ACS1 combination, p415ADH-ALD2, p416ADH-ACS1 combination, or p415ADH-ALD3, p416ADH-ACS1 combination. However, no transformant was obtained in the CC02-0257 strain having triple defects in PDC genes where no PDC activity was exhibited. The thus-prepared strains and their genetic traits and summarized in Table 11. An evaluation of lactic acid fermentation-ability for the ALD and ACS1 overexpressing strains, prepared in Example 7, was conducted. Specifically, the yeast was inoculated into each flask containing 25 ml of the medium, prepared in Example 3 for the purpose of lactic acid fermentation evaluation and was cultured under aerobic condition at 30 for 71 hours. The amount of D-type lactic acid present in the fermented broth was analyzed, and an enzymatic analysis (Acetic acid, R-Biophartn, Germany was conducted to determine the amount of acetic acid present therein. The above experiment results are summarized in Table 12 below. As verified in Table 12, the strains having decreased PDC5 activity by IDP2 promoter or SCO2 promoter had a dramatic reduction in the accumulation of the acetate, a by-product, i.e., little detection of acetate was confirmed, compared to the strain with normal PDC5 activity. In such case, the final cell concentration of the strains, in which the activities of ALD and ACS were not increased, tended to decrease according to the PDC5 promoter substitutions. On the contrary, the strains, where the PDC5 expression was reduced and the activities of ALD and ACS were increased, showed an increase in the final cell concentration. Accordingly, the improvement in the cell growth was confirmed. Specifically, the strains of CC02-0277 and CC02-0278 having increased ALD and ACS activities prepared based on the CC02-0170 strain, where PDC5 promoter was substituted with IDP2, showed improved growth rate, D-lactic acid concentration of production, production yield thereof, and fermentation productivity as increasing in the-ALD and ACS activities. In summary, the strain where PDC5 was substituted with a weak expression of IDP2 had a reduction in acetate accumulation, and the final OD was 1.3 times higher compared to the strain exhibiting normal expression of PDC5. In addition, it was confirmed that, when ALD and ACS were co-expressed under the control of the ADH1 promoter, the glucose consumption and the rate thereof were increased, and finally, the percentage yield was increased from 56% or %59?/ to 66% or 67%, respectively, showing improved yield. Specifically, by comparing the two kinds of promoters applied to the weak expression of PDC5, it was confirmed that, the lactic acid productivity was improved in both strains having SCO2 promoter and IDP2 promoter, respectively. However, the strain having IDP2 promoter may be considered as the most optimized form of a strain in terms of the overall cell concentration, the glucose consumption, and the rate thereof. Since the effects of the cell growth and the yield improvements resulted from the decreased PDC5 activity have been clearly confirmed, an evaluation as undertaken to determine the effects of additional PDC gene defect in lactic acid production. The evaluation method for each strain was identical to the method described in Example 8 and the culturing was conducted for 74 hours. The thus-obtained experiment results are summarized in Table 13 below. As confirmed in Table 13, the acetate concentration was clearly reduced in the strains having double defects in PDC1 and PDC5 genes, however, a reduction in the D-lactic acid concentration of production was also observed due to the reduction in the cell growth and the glucose consumption. In addition, the strain where the PDC pathway is almost inactivated, which was resulted from the double defects in PDC1 and PDC5 genes, did not have any improvement in the cell growth, the glucose consumption;and the productivity thereof, although the strain exhibited increased activities of ALD and ACS. For the purpose of a fermentation evaluation using sucrose, the lactic acid-producing yeast strains, where PDC pathway is attenuated, the identical strains evaluated in Example 8 and 9 were used to confirm the effect of the lactic acid production. In this regard, sucrose was employed as a carbon source instead of glucose. The evaluation method was performed in the same manner as Example 8. The thus-obtained experiment results re summarized in Table 14 below. The use of sucrose instead of glucose for the strains, used in the same manner as in Examples 8 and 9, allowed for improved effects of the growth and fermentation yield by increasing the activities of ALD and ACS in the strains where PDC pathway is attenuated, showing the same pattern of results as the strains in Example 8 where glucose was employed as a carbon source. Accordingly, the present invention confirms that the improved effects of fermentation yield and growth due to the decreased PDC activity and increased ALD and ACS activities, which were confirmed in the present invention, are not limited to the type of sugar used. To summarize the above results, it was confirmed that, when the strains were mutated in such a way that PDC pathway was attenuated, and the activities of ALD and ACS were improved compared to that of the non-mutated strains, the lactic acid production was increased, and the growth rate thereof was maintained simultaneously. From the foregoing, a skilled person in the art to which the present invention pertains will be able to understand that the present invention may be embodied in other specific forms without modifying the technical concepts or essential characteristics of the present invention. In this regard, the exemplary embodiments disclosed herein are only for illustrative purposes and should not be construed as limiting the scope of the present invention. On the contrary, the present invention is intended to cover not only the exemplary embodiments but also various alternatives, modifications, equivalents and other embodiments that may be included within the spirit and scope of the present invention as defined by the appended claims. The present invention relates to Saccharomyces sp. capable of producing lactic acid with a decreased activity of pyruvate decarboxylase (PDC) and increased activities of aldehyde dehydrogenase (ALD) and acetyl-CoA synthetase (ACS), and a method of producing lactic acid from the culture medium obtained by culturing the microorganism. 1. An isolated a) the activity of pyruvate decarboxylase (PDC) of the microorganism is decreased compared to that of a non-modified lactic acid-producing strain; and b) the activities of aldehyde dehydrogenase (ALD) and acetyl-CoA synthetase (ACS) of the microorganism are enhanced compared to that of the non-modified lactic acid-producing strain. 2. The microorganism according to 3. The microorganism according to i) inactivate PDC1 activity and decrease PDC5 activity; or ii) decrease PDC 1 activity and inactivate PDC 5 activity. 4. The microorganism according to 5. The microorganism according to 6. The microorganism according to 7. A method for producing lactic acid comprising:
a) culturing the microorganism according to b) recovering lactic acid from the culture medium or the microorganism in step a). 8. A method for producing lactic acid comprising:
a) culturing the microorganism according to b) recovering lactic acid from the culture medium or the microorganism in step a). 9. A method for producing lactic acid comprising:
a) culturing the microorganism according to b) recovering lactic acid from the culture medium or the microorganism in step a). 10. A method for producing lactic acid comprising:
culturing the microorganism according to b) recovering lactic acid from the culture medium or the microorganism in step a). 11. A method for producing lactic acid comprising:
a) culturing the microorganism according to b) recovering lactic acid from the culture medium or the microorganism in step a). 12. A method for producing lactic acid comprising:
a) culturing the microorganism according to b) recovering lactic acid from the culture medium or the microorganism in step a).TECHNICAL FIELD
BACKGROUND ART
DISCLOSURE
Technical Problem
Technical Solution
Advantageous Effects
BRIEF DESCRIPTION OF DRAWINGS
BEST MODE FOR CARRYING OUT INVENTION
EXAMPLE 1
Preparation of Lactic Acid-Producing Strain
Primers used for the production of the base yeast strain Primer 5′ -> 3′ sequence ADH1 upstream CGGGATCCACTGTAGCCCTAGACTTGATAGCC forward primer (SEQ ID NO: 1) ADH1 upstream ATAAGAATGCGGCCGCTGTATATGAGATAGTTGATTGTAT reverse primer GCTT (SEQ ID NO: 2) ADH1 downstream GACTAGTGCGAATTTCTTATGATTTATGATTTTTATT forward primer (SEQ ID NO: 3) ADH1 downstream ACATGCCATGgAAGCATGCACGTATACACTTGAGTAA reverse primer (SEQ ID NO: 4) PDC1 upstream CGGGATCCATTATGTATGCTCTTCTGACTTTTCGT forward primer (SEQ ID NO: 5) PDC1 upstream ATAAGAATGCGGCCGCTTTGATTGATTTGACTGTGTTATT reverse primer TTGC (SEQ ID NO: 6) PDC1 downstream CGGGATCCGCGATTTAATCTCTAATTATTAGTTAAAG forward primer (SEQ ID NO: 7) PDC1 downstream ATAAGAATGCGGCCGCTTTCAATCATTGGAGCAATCATT reverse primer TTACA (SEQ ID NO: 8) DLD1-HIS3 upstream GCGTAGTTGGCCCCAACTGGTGCAGTAATACGTTTTAAG linking primer AGCTTGGTGAG (SEQ ID NO: 9) DLD1-HIS3 CGTGAAGGGTGAAAAAGGAAAATCAGATACCTACATAA downstream linking GAACACCTTTGG primer (SEQ ID NO: 10) EXAMPLE 2
Preparation of Mutant Strains having Decreased PDC5 Activity
Primers used for the preparation of promoter-substituted strains Primers 5′ -> 3′ sequence F_PDC5_UP_676 GTCAGCATTGACACGTTCGATT (SEQ ID NO: 11) R_K1URA3-PDC5_UP TCTACCCAGAATCACTTCTTTCGAGAGATTGTCATAAT (SEQ ID NO: 12) C F_PDC5_UP- CAATCTCTCGAAAGAAGTGATTCTGGGTAGAAGATCG AL_K1URA3 G (SEQ ID NO: 13) R_AL_K1URA3 GAGCAATGAACCCAATAACGAAATCTT (SEQ ID NO: 14) F_BR_K1URA3 CTTGACGTTCGTTCGACTGATGAG (SEQ ID NO: 15) R_PDC5_DOWN_522 CAAGTCAACCAAGTTAGCTGGC (SEQ ID NO: 16) R_SCO1p-BR_K1URA3 CTCTCCTAATAGACGTGGTGTCACCATGAACGACAATT (SEQ ID NO: 17) CTTAA F_SCO1p_500 CGTTCATGGTGACACCACGTCTATTAGGAGAGCCATTC (SEQ ID NO: 18) R_PDC5_DOWN_500- AAGGTTATTTCAGACATCTTTTCTACGTTTGCTGTTTTT SCO1p TC (SEQ ID NO: 19) F_SCO1p- CAGCAAACGTAGAAAAGATGTCTGAAATAACCTTAGG PDC5_DOWN_500 TAAAT (SEQ ID NO: 20) R_SCO2p-BR_K1URA3 ATCGAATAAGTAACAAGCGTGTCACCATGAACGACAA (SEQ ID NO: 21) TTCTTAA F_SCO2p_500 CGTTCATGGTGACACGCTTGTTACTTATTCGATAACGC (SEQ ID NO: 22) R_PDC5_DOWN_500- AAGGTTATTTCAGACATTTTACTCTCGCTTCCCAAATT SCO2p CC (SEQ ID NO: 23) F_SCO2p- GGAAGCGAGAGTAAAATGTCTGAAATAACCTTAGGTA PDC5_DOWN_500 AAT (SEQ ID NO: 24) R_IDP2p-BR_K1URA3 TAAAAATAAATAGATAGACGTGTGTCACCATGAACGA (SEQ ID NO: 25) CAATTCTTAA F_IDP2p_500 CGTTCATGGTGACACACGTCTATCTATTTATTTTTATAA (SEQ ID NO: 26) CTC R_PDC5_DOWN_500- AAGGTTATTTCAGACATTACGATTTTATATATATACGTA IDP2p CGTTA (SEQ ID NO: 27) F_IDP2p- CGTATATATATAAAATCGTAATGTCTGAAATAACCTTAG PDC5_DOWN 500 GTAAAT (SEQ ID NO: 28) R_ACS1p-BR_K1URA3 CTGGACGTATGTGCACAGTGTCACCATGAACGACAAT (SEQ ID NO: 29) TCTTAA F_ACS1p_500 CGTTCATGGTGACACTGTGCACATACGTCCAGAATGAT (SEQ ID NO: 30) R_PDC5_DOWN_500- AAGGTTATTTCAGACATAGCACAGTGGGCAATGTCTTT ACS1p C (SEQ ID NO: 31) F_ACS1p- CATTGCCCACTGTGCTATGTCTGAAATAACCTTAGGTA PDC5_DOWN_500 AAT (SEQ ID NO: 32) R_FBA1p-BR_K1URA3 TTATTTACGTAATGACCCAGTGTCACCATGAACGACAA (SEQ ID NO: 33) TTCTTAA F_FBA1p_500 CGTTCATGGTGACACTGGGTCATTACGTAAATAATGAT (SEQ ID NO: 34) AG R_PDC5_DOWN_500- AAGGTTATTTCAGACATTTTGAATATGTATTACTTGGTT FBA1p ATGGT (SEQ ID NO: 35) F_FBA1p- CCAAGTAATACATATTCAAAATGTCTGAAATAACCTTA PDC5_DOWN_500 GGTAAAT (SEQ ID NO: 36) PDC5 promoter-mutated strains Strains Genetic Traits CC02-0167 CC02-0064 PDC5 promoter::KlURA3-SCO1 promoter CC02-0168 CC02-0064 PDC5 promoter::KlURA3-SCO2 promoter CC02-0169 CC02-0064 PDC5 promoter::KlURA3-ACS1 promoter CC02-0170 CC02-0064 PDC5 promoter::KlURA3-IDP2 promoter CC02-0174 CC02-0064 PDC5 promoter::KlURA3-FBA1 promoter EXAMPLE 3
Evaluation of Lactic Acid Fermentation for Mutant Strains having Decreased PDC5 Activity
Evaluation of lactic acid fermentation for PDC5 promoter-mutated strains 24 hours 48 hours Glucose Lactic Glucose Lactic Yield Strain OD Consumed acid OD Consumed acid (%) CC02- 3.9 15.0 10.9 8.7 63.4 41.6 65.7 0064 CC02- 5.7 25.0 19.8 9.4 69.9 47.3 67.7 0174 EXAMPLE 4
Preparation of a Strain having a PDC5 Gene Defect
Primers used for the preparation of the strain having PDC5 defects Primers 5′ -> 3′ Sequence F-ALPDC5- GAGCTCGGATCCAAGGAAATAAAGCAAATAACAATAACACC BamHI (SEQ ID NO: 37) R-ALPDC5- ACCATGGCGGCCGCTTTGTTCTTCTTGTTATTGTATTGTGTTG NotI (SEQ ID NO: 38) F-BRPDC5- GGATCCACTAGTGCTAATTAACATAAAACTCATGATTCAACG SpeI (SEQ ID NO: 39) R-BRPDC5- CAGCTGCCATGGTATTCTAAATAAGATGTAAGGCCTTGTAAT NcoI (SEQ ID NO: 40) EXAMPLE 5
Preparation of PDC1 promoter-mutated strains based on the strain having a PDC5 defect
Primers used for preparation of the strains having a PDC5 defect and decreased PDC1 activity Primers 5′ -> 3′ Sequence F_PDC1 ATAACTAGTATGTCTGAAATTACTTTGGGTAAAT (SEQ ID NO: ATTT 41) R_PDC1 CAAAGGAAAAGGGGCCTGTTTATTGCTTAGCGTTG (SEQ ID NO: GTAGCAGCA 42) F_CYC1t TACCAACGCTAAGCAATAAACAGGCCCCTTTTCCTT (SEQ ID NO: TGTCGAT 43) R_CYC1t ATACTCGAGGCAAATTAAAGCCTTCGAGCGTCC (SEQ ID NO: 44) F_PDC1p AAAGAGCTCCATGCGACTGGGTGAGCATATGTT (SEQ ID NO: 45) R_PDC1p ATAACTAGTTTTGATTGATTTGACTGTGTTATTTT (SEQ ID NO: GC 46) F_IDP2p AAAGAGCTCACGTCTATCTATTTATTTTTATAACT (SEQ ID NO: CC 47) R_IDP2p ATAACTAGTTACGATTTTATATATATACGTACGTT (SEQ ID NO: AC 48) Strains having PDC5 defect and decreased PDC1 activity Strains Genetic Traits CC02-0450 CC02-0064 pdc5Δ CC02-0451 CC02-0450 PDC1p-PDC1-CYC1t CC02-0452 CC02-0450 IDP2p-PDC1-CYC1t EXAMPLE 6
Preparation of Strains having Double or Triple Defects in PDC Genes
Primers used for preparation of the strains having double or triple defects in PDC genes Primers 5′ -> 3′ Sequence F_BamHI- CGGGATCCAGGCCAAGGAAATAAAGCAAATAACAA PDC5_1513 (SEQ ID. 49) R_NotI-PDC5_UP ATAAGAATGCGGCCGCTTTGTTCTTCTTGTTATTGTATTGTG (SEQ ID NO: 50) TT F_BamHI- CGGGATCCGCTAATTAACATAAAACTCATGATTCAA PDC5_DOWN (SEQ ID NO: 51) R_NotI- ATAAGAATGCGGCCGCTATTCTAAATAAGATGTAAGGCCTT PDC5_DOWN GTA (SEQ ID NO: 52) F_PDC5_UP AGGCCAAGGAAATAAAGCAAATAACAA (SEQ ID NO: 53) R_AL_K1URA3 GAGCAATGAACCCAATAACGAAATCTT (SEQ ID NO: 54) F_BR_K1URA3 CTTGACGTTCGTTCGACTGATGAG (SEQ ID NO: 55) R_PDC5_DOWN TATTCTAAATAAGATGTAAGGCCTTGTA (SEQ ID NO: 56) F_BamHI- CGGGATCCTGTTATAGAGTTCACACCTTATTCACA PDC6_UP (SEQ ID NO: 57) R_NotI-PDC6_UP ATAAGAATGCGGCCGCTTTGTTGGCAATATGTTTTTGCTATA (SEQ ID NO: 58) TTA F_BamHI- CGGGATCCGCCATTAGTAGTGTACTCAAACGAAT PDC6_DOWN (SEQ ID NO: 59) R_NotI- ATAAGAATGCGGCCGCGATGCAGAATGAGCACTTGTTATTT PDC6_DOWN AT (SEQ ID NO: 60) F_PDC6_UP TGTTATAGAGTTCACACCTTATTCACA (SEQ ID NO: 61) R_AL_K1URA3 GAGCAATGAACCCAATAACGAAATCTT (SEQ ID NO: 62) F_BR_K1URA3 CTTGACGTTCGTTCGACTGATGAG (SEQ ID NO: 63) R_PDC6_DOWN GATGCAGAATGAGCACTTGTTATTTAT (SEQ ID NO: 64) Strains having double or triple defects in PDC genes Strains Genetic traits CC02-0256 CC02-0064 pdc5Δ CC02-0257 CC02-0256 pdc6Δ EXAMPLE 7
Preparation of ALD and ACS1 Overexpressing Strains
Primers used for the preparation of ALD and ACS1 overexpressing strains Primers 5′ -> 3′ Sequence F_SpeI_ALD2 CAAGCTGGCCGCTCTAGAACTAGTATGCCTACCTTGTATACT (SEQ ID NO: 65) GATATCGA R_XhoI_ALD2 ACATAACTAATTACATGACTCGAGTTAGTTGTCCAAAGAGAG (SEQ ID NO: 66) ATTTATGT F_SpeI_ALD3 CAAGCTGGCCGCTCTAGAACTAGTATGCCTACCTTGTATACT (SEQ ID NO: 67) GATATCGA R_XhoI_ALD3 ACATAACTAATTACATGACTCGAGTTATTTATCCAATGAAAGA (SEQ ID NO: 68) TCCACAT F_SpeI_ACS1 TCCAAGCTGGCCGCTCTAGAACTAGTATGTCGCCCTCTGCCG (SEQ ID NO: 69) TACA R_EcoRI_ACS1 TATCGATAAGCTTGATATCGAATTCTTACAACTTGACCGAATC (SEQ ID NO: 70) AATTAGA ALD and ACS overexpressing strains Strains Genetic Traits CC02-0225 CC02-0064 p415ADH, p416ADH CC02-0226 CC02-0064 p415ADH-ALD2, p416ADH-ACS1 CC02-0227 CC02-0064 p415ADH-ALD3, p416ADH-ACS1 CC02-0356 CC02-0168 p414ADH, p415ADH CC02-0275 CC02-0168 p414ADH-ACS1, p415ADH-ALD2 CC02-0276 CC02-0168 p414ADH-ACS1, p415ADH-ALD3 CC02-0357 CC02-0170 p414ADH, p415ADH CC02-0277 CC02-0170 p414ADH-ACS1, p415ADH-ALD2 CC02-0278 CC02-0170 p414ADH-ACS1, p415ADH-ALD3 CC02-0444 CC02-0256 p415ADH, p416ADH CC02-0361 CC02-0256 p415ADH-ALD2, p416ADH-ACS1 CC02-0362 CC02-0256 p415ADH-ALD3, p416ADH-ACS1 CC02-0453 CC02-0451 p414ADH, p415ADH CC02-0454 CC02-0451 p414ADH-ACS1, p415ADH-ALD2 CC02-0455 CC02-0451 p414ADH-ACS1, p415ADH-ALD3 CC02-0456 CC02-0452 p414ADH, p415ADH CC02-0457 CC02-0452 p414ADH-ACS1, p415ADH-ALD2 CC02-0458 CC02-0452 p414ADH-ACS1, p415ADH-ALD3 EXAMPLE 8
Evaluation of Lactic Acid Fermentation for the Yeast Strains
Evaluation of the growth rate, lactic acid fermentation, by-products, and production yield, etc., for the ALD and ACS overexpressing strains Initial Residual D-lactic Produc- Final glucose glucose Acetate acid Yield tivity Strains OD (g/L) (g/L) (g/L) (g/L) (g/g) (g/l · h) CC02- 9.3 88 10 2.87 41.1 0.53 0.579 0225 CC02- 9.3 83 10.5 2.91 42.4 0.59 0.597 0226 CC02- 10.1 84 9.5 2.91 41.8 0.56 0.589 0227 CC02- 6.9 88 26 0.02 27.6 0.45 0.389 0356 CC02- 11.6 88 11.5 0.01 47.6 0.62 0.670 0275 CC02- 10.6 88 11 0.01 46.8 0.61 0.659 0276 CC02- 12.2 88 13 0.04 38.1 0.51 0.537 0357 CC02- 17.8 88 1 0.03 58.6 0.67 0.825 0277 CC02- 18.8 88 0 0.02 56.9 0.66 0.801 0278 CC02- 9.8 88 8.5 2.2 38.9 0.49 0.548 0453 CC02- 10.2 88 8.1 2.4 39.5 0.49 0.556 0454 CC02- 9.2 88 8.8 2.1 40 0.51 0.563 0455 CC02- 12 88 10.1 0.02 38.5 0.49 0.542 0456 CC02- 18.1 88 0 0.02 55.8 0.63 0.786 0457 CC02- 18.5 88 0 0.02 56.5 0.64 0.800 0458 EXAMPLE 9
Evaluation of Lactic Acid Fermentation for the Yeast Strain having Double Defects in PDC1 and PDC5 Genes, and Increase in ALD and ACS Activities
The evaluation results of lactic acid fermentation for the strains having double defects in PDC1 and PDC5 genes Initial Residual D-lactic Produc- Final Glucose Glucose Acetate acid Yield tivity Strains OD (g/L) (g/L) (g/L) (g/L) (g/g) (g/l · h) CC02- 3.2 78.5 52 0.10 20.8 78.5 0.281 0444 CC02- 3.9 78.5 49 0.05 25.4 86.3 0.343 0361 CC02- 3.8 78.5 51 0.08 22.8 82.8 0.308 0362 EXAMPLE 10
Evaluation of Lactic Acid Fermentation for the Strains, Where PDC Pathway is Attenuated, Using Sucrose
The evaluation results of lactic acid fermentation for the strains having double defects in PDC1 and PDC5 genes or decreased PDC5 activity Initial Residual D-lactic Produc- Final Glucose Glucose Acetate acid Yield tivity Strains OD (g/L) (g/L) (g/L) (g/L) (g/g) (g/l · h) CC02- 5.15 91.5 27.5 1.95 25.19 39.36 0.34 0225 CC02- 6.9 91.5 15 1.92 30.89 40.38 0.42 0226 CC02- 6.18 91.5 15 1.98 29.59 38.68 0.40 0227 CC02- 1.6 91.5 26.75 0.02 11.72 18.11 0.16 0356 CC02- 1.88 91.5 21.75 0.02 13.79 19.77 0.19 0275 CC02- 2.2 91.5 18.25 0.01 16.04 21.9 0.22 0276 CC02- 2.78 91.5 22 0.03 17.08 24.58 0.23 0357 CC02- 12.15 91.5 7.75 0.02 44.65 53.31 0.60 0277 CC02- 11.88 91.5 6.25 0.01 43.84 51.43 0.60 0278 CC02- 2.45 91.5 37 0.02 21.94 40.25 0.30 0444 CC02- 2.5 91.5 18.25 0.02 21.73 29.66 0.29 0361 CC02- 3.08 91.5 15.25 0.02 24.92 32.67 0.34 0362
