KR100730315B1 - Method for Manufacturing Xylitol with High-Yield - Google Patents

Abstract

The present invention relates to a method for producing xylitol in high yield using xylitol producing strains in which the expression of xylitol dehydrogenase is suppressed. In the high yield production method of xylitol of the present invention, a part of the xylitol dehydrogenase gene is non-specifically deleted, substituted or added to the xylitol producing strain in which the expression of xylitol dehydrogenase is suppressed. Inoculating a medium containing the, and culturing until the entire amount of xylose contained in the medium, and then comprises the step of obtaining xylitol therefrom. When the high yield production method of xylitol of the present invention is used, xylitol can be produced in a higher yield than the conventional production method, and thus it can be widely used in the manufacture of various foods, medicines and the like including xylitol.

Xylitol, xylose, xylitol dehydrogenase, xylitol producing strain

Description

Method for Manufacturing Xylitol with High-Yield

1 is a genetic map of the transformation vector pXYL2-Ura3.

2 is a graph showing the change in concentration of dry cells, glucose, glycerol, xylose and xylitol over time when glycerol is produced using glycerol as a carbon source.

The present invention relates to a high yield production method of xylitol. More specifically, the present invention relates to a method for producing xylitol in high yield using xylitol producing strains in which the expression of xylitol dehydrogenase is suppressed.

Xylitol is an pentose sugar alcohol that has high sweetness and is widely used as a functional sweetener to replace sugar. Xylitol is similar to sugar in sweetness and twice as high as sorbitol, and also has a refreshing feeling in the mouth due to the heat loss when melting heat is only 1/3 of the sugar and the heat of dissolution is 153 J / g. It is used as a sugar-free raw material for confectionery products. In addition, since the metabolic process after ingestion in the body is independent of insulin, it is used as a substitute sugar for diabetic patients. In particular, it has a characteristic of inhibiting the growth of Streptococcus mutans , which is a caries-inducing bacterium, and is widely used in toothpaste and the like as a tooth decay suppressing component.

In order to produce such xylitol, a method of reducing xylose by hydrogenation was used as a chemical method, but the production yield is not high as 50 to 60%, and the process of separating and purifying the product is complicated and expensive. Since the process is a high temperature and high pressure, there is a high risk, there was a lot of waste. In recent years, intensive research has been conducted on xylitol production methods by biological methods to compensate for these disadvantages. For example, Korean Patent Registration No. 199819 discloses xylitol by converting xylose to xylitol by culturing a new strain Candida tropicalis isolated from natural sludge in a medium containing xylose, a nitrogen source, and an inorganic salt. A method of producing is disclosed. The biological xylitol manufacturing method can use relatively low purity xylose as a raw material as compared to the chemical method, and after the production of xylitol, xylose is completely consumed. It can be lowered, and the process itself is safe at room temperature and pressure, so it is safe and does not discharge waste. However, the yield of xylitol is only about 70-80%, and efforts are being made to further improve the yield, but there are no results.

Therefore, there is a constant need to develop a method for improving the yield of xylitol by a biological method.

Accordingly, the present inventors have made intensive studies to develop a method for improving the yield of xylitol by a biological method. When a part of the xylitol dehydrogenase gene is deleted and the expression of xylitol dehydrogenase is suppressed, It was confirmed that xylitol can be produced in high yield, and thus the present invention was completed.

After all, the main object of the present invention is to provide a method for producing xylitol in high yield using a xylitol producing strain in which the expression of xylitol dehydrogenase is suppressed.

In the high yield production method of xylitol of the present invention, a part of the xylitol dehydrogenase gene is non-specifically deleted, substituted or added to the xylitol producing strain in which the expression of xylitol dehydrogenase is suppressed. Inoculating a medium comprising a cow, culturing until the entire amount of xylose contained in the medium is consumed, and then obtaining xylitol therefrom. At this time, the xylitol producing strain is not particularly limited, but it is preferable to use a strain of the genus Candida, more preferably Candida guillermondi ( C. guillermondi ), Candida parapsilosis ( C. parapsilosis ) or Candida tropicalis ( C. tropicalis ). In addition, the carbon source is not particularly limited thereto, but it is preferable to use glycerol, fructose, galactose, sugar, mannose, maltose, cellobiose, or mixtures thereof, and the nitrogen source is not particularly limited thereto. Preferably, the trace element is not particularly limited, but potassium diphosphate, magnesium sulfate or a mixture thereof is preferably used. In addition, the culture conditions of the xylitol producing strain is not particularly limited, but is preferably cultured at 20 to 40 ℃.

Hereinafter, a high yield production method of xylitol of the present invention will be described in more detail.

As a method for biologically preparing xylitol, a method of culturing Candida genus in a medium containing xylose and obtaining xylitol from the cultured strain has been used. From what the studies so far, the syntax boiler Mondi Candida (C. guillermondi), Candida parapsilosis (C. parapsilosis), Candida sp, such as Candida Tropical faecalis (C. tropicalis) is a xylose absorption in the extracellular Treated with xylose reductase to convert to xylitol, treated with xylitol dehydrogenase, converted to xylulose, and electro-xylulose is converted back to xylulose kinase (xylulose kinase) is converted to xylulose-5-phosphate, which is known to continue to be used for cell growth and maintenance via the pentose phosphate pathway. JM et al., Appl.Microbiol.Biotechnol., 36: 158-162, 1991; Hahn-Hagerdal, B. et al., Enzyme Microb.Technol., 16: 933-943, 1994).

Accordingly, the present inventors pay attention to the fact that xylitol produced in the strain of the genus Candida is converted to xylulose by xylitol dehydrogenase, and by inhibiting the activity or suppressing the expression of the xylitol dehydrogenase produced from xylose, Since xylitol is no longer used for cell growth and maintenance, it was theoretically assumed that it would be able to produce xylitol in a yield of 100%.

To clone the unknown Candida Tropicalis xylitol dehydrogenase, the inventors have previously discovered a group of medium-chain alcohol dehydrogenases, a group of known xylitol dehydrogenases and similar enzymes of Pichia stipitis. Compare gene homology between genes belonging to sorbitol dehydrogenase, alcohol dehydrogenase, threonine dehydrogenase, etc. The gene amplification technique (PCR) used as a template obtained 1,095 bp of xylitol dehydrogenase gene of Candida Tropicalis. A non-specifically deleted, substituted or added portion of the previously obtained gene was constructed to produce a modified gene that does not normally express xylitol dehydrogenase, and then introduced it into normal Candida tropical cells, followed by homologous recombination. Genes are selectively removed through an intracellular mechanism, such that a transgenic strain can not be grown in a medium containing only xylose as a carbon source.

The previously constructed transformed strains were cultured in a liquid medium consisting of glucose, xylose, yeast extract, potassium diphosphate and magnesium sulfate, and consumed 12.5 g / L xylose to produce 12.5 g / L xyitol. Xylitol could be produced from xylose in 100% yield. However, not all of the xylose in the medium was converted to xylitol, which was analyzed that glucose used as a carbon source did not provide enough intracellular reducing power for the production of xylitol. Accordingly, as a result of searching for a carbon source capable of supplying enough reducing power for xylitol production to various carbon sources, it was found that glycerol, sugar, mannose, maltose and cellobiose are effective carbon sources for the production of xylitol. In particular, it was confirmed that glycerol can effectively produce xylitol even if it contains a relatively small amount in the medium compared to other carbon sources.

As a result, when cultured transgenic strains of Candida tropicalis in a medium containing xylose precursor xylose and carbon source glycerol, it was possible to produce xylitol in a yield of about 97 to 100%.

Therefore, when the high yield production method of xylitol of the present invention is used, xylitol can be produced at a higher yield than the conventional production method, and thus it can be widely used for the production of various foods, medicines and the like including xylitol.

Hereinafter, the present invention will be described in more detail with reference to Examples. These examples are only for illustrating the present invention in more detail, and it will be apparent to those skilled in the art that the scope of the present invention is not limited to these examples according to the gist of the present invention. Particularly, in the following examples, a method of constructing a transformant that inhibits the expression of xylitol dehydrogenase of Candida tropicalis and using the same, has been disclosed. The method for producing xylitol in high yield is disclosed. Only one embodiment, it will be apparent that the scope of the present invention is not limited thereto.

Example 1 Construction of Transformed Candida Tropicalis with Inhibited Expression of Xylose Dehydrogenase

The genomic DNA of Candida tropicalis ( C. tropicalis ) as a template, PCR (94 ℃ 1 min, 25 repetitions (94 ℃ 30 seconds, 58 ℃ 30 seconds, 72 ℃ 30 seconds) and 72 ℃ using the following primers 3 min) to amplify the genes of xylitol dehydrogenase of Candida tropicalis, clone the gene of the amplified Candida tropicalis xylitol dehydrogenase into pGEM-T easy vector (BIONEX, Korea), The BamHI locus was introduced in the middle of the dehydrogenase gene, and the ura3 gene was introduced into the previously introduced BamHI locus, thereby obtaining a transformation vector pXYL2-Ura3 of 4.7 kb (see Fig. 1). 1 is a genetic map of a transformed pXYL2-Ura3 vector.

primer F: 5'-aatggtcttgggtcacgaatcc-3 '(SEQ ID NO: 1)

primer R: 5'-gctctgaccaagtcgtaggcttc-3 '(SEQ ID NO: 2)

The vector pXYL2-Ura3 obtained above was introduced into Candida Tropicalis, and this was selected as a solid medium for screening (urag-free) (yield nitrogen base (amino acid free) 6.7 g / L, glucose 20 g / L, agar powder 15 g). / L) and incubated at 30 ° C. for 2 days. Then, the colonies formed in the solid medium were separated into solid medium containing xylose (yield nitrogen base (non-amino acid) 6.7 g / L, xylose 20 g / L, agar powder 15 g / L) and glucose containing solid medium (yeast) Inoculated in nitrogen base (non-amino acid) 6.7g / L, glucose 20g / L, agar powder 15g / L) and incubated at 30 ° C. for 2 days, and did not grow in a solid medium containing xylose, containing glucose Strains growing only in solid medium were selected to obtain Candida Tropicalis (hereinafter referred to as "BS-xdh" for convenience) from which xylitol dehydrogenase was removed.

Example 2 Preparation of Xylitol Using a Transformant

The transformant BS-xdh constructed in Example 1 was inoculated in 3 ml of YM medium (20 g / L glucose, 3 g / L yeast extract, 3 g / L malt extract and 5 g / L peptone), and at 200 rpm at 30 ° C. Samples (samples 1 to 3) were obtained at 6 hour intervals while incubating for 12 hours with shaking.

Subsequently, 1 ml of the electroculture solution was inoculated into 50 ml of production medium (10 g / L glucose, 10 g / L yeast, 10 g / L yeast extract, 5 g / L potassium diphosphate and 0.2 g / L magnesium sulfate, pH 5.0), Samples (Samples 4 to 7) were obtained at 6 hour intervals with shaking culture at 200 ° C. at 200 rpm for 24 hours.

For each of the samples 1 to 7 obtained above, dry cell concentration (weight of dry cells per 1 L of culture medium) and xylose concentration (weight of g of xylose per 1 L of culture medium) were measured, respectively. That is, the dry cell concentration was calculated by measuring the absorbance at 600 nm by applying an electric sample to a spectrophotometer (Shimrozu, Japan) and converting it into a standard curve analyzed beforehand. In addition, centrifugation of the electrical sample to obtain a supernatant, which was HPLC (Shimazu, Japan) system (Sugar-Pak I column (Waters, USA), refracive index detector (Waters, USA), solvent: water, flow rate: 0.5 ml / min, column temperature: 90 ° C.) to determine the concentration of xylose.

Meanwhile, the cells obtained by centrifuging each sample were centrifuged to obtain a supernatant, and then the concentration of xylitol (weight of g of xylitol per liter of culture solution (g)) was measured by applying an HPLC system (see Table 1). ).

Changes of Dry Cell, Xylose and Xylitol Concentrations According to Incubation Time sample Incubation time (h) Dry cell concentration (g / L) Xylose Concentration (g / L) Xylitol Concentration (g / L) One 0 0.10 45.4 0.0 2 6 0.52 45.3 0.0 3 12 2.63 45.3 0.0 4 18 6.76 37.5 7.8 5 24 6.65 32.9 12.5 6 30 6.55 32.9 12.4 7 36 6.58 32.8 12.4

As shown in Table 1, since the amount of xylitol was consumed as xylose was produced, the yield of xylitol was found to reach 100%. However, after incubation for 24 hours, it was found that xylose was no longer consumed in the medium and xylitol was no longer produced. At this time, the utilization rate of xylose in the medium was only about 28%, It was found that the xylose contained in the medium was not sufficiently utilized.

Example 3 Screening of Carbon Sources That Can Improve the Utilization of Xylose

First, the transformant BS-xdh prepared in Example 1 was inoculated in 3 ml of YM medium, and cultured for 12 hours while shaking at 200 rpm at 30 ° C.

Subsequently, 1 ml of the electroculture solution was used instead of glucose, and various carbon sources (mannose, fructose, galactose, maltose, sugar, lactose, cellobiose, meliobios, glycerol, acetic acid, gluconic acid, propio) 50 ml of the production medium containing nitric acid (propionic acid or malic acid) was inoculated and incubated for 96 hours while shaking at 200 rpm at 30 ° C.

After the incubation was completed, using the same method as in Example 1, the dry cell concentration (A), the concentration of carbon source consumed in the culture (B), the concentration of xylose consumed in the culture (C) and the produced The concentration of xylitol (D) was measured, the concentration of xylose consumed was divided by the concentration of xylose contained in the medium at the beginning of the culture, and the utilization rate of xylose (E) was calculated. Xylitol yield (F) was calculated by dividing by the concentration of xylose and compared with each other (see Table 2). At this time, the concentration of the carbon source in the culture, the concentration of xylose consumed in the culture and the concentration of xylitol produced were measured using the HPLC system of Example 2.

Dry cell concentration according to carbon source (A), concentration of carbon source consumed (B), concentration of xylose consumed (C), concentration of xylitol produced (D), utilization of xylose (E) and xylitol yield (F) ) Change Carbon source A (g / L) B (g / L) C (g / L) D (g / L) E (%) F (%) Mannose 2.9 9.0 36.4 36.3 72.8 99.6 fruit sugar 5.3 8.9 23.3 23.6 46.6 101.2 Galactose 2.7 9.2 26.0 27.0 52.0 103.6 Maltose 2.2 8.3 29.9 27.2 59.8 90.9 Sugar 4.4 8.9 35.5 36.0 71.0 101.3 Lactose 0.4 0.1 2.5 2.7 5.0 108.0 Cellobios 3.5 9.1 39.4 38.3 78.8 97.2 Meliobios 1.1 1.6 5.0 4.0 10.0 80.0 Glycerol 3.2 9.1 45.2 46.2 90.4 102.3 Acetic acid 1.0 9.0 11.0 12.3 22.0 112.1 Gluconic Acid 1.0 2.1 3.9 4.0 7.8 102.2 Propionate 2.6 1.9 1.7 1.7 3.4 100.0 Malic acid 2.1 0.9 4.0 4.1 8.0 102.4

As shown in Table 2, when glycerol, fructose, galactose, sugar, mannose, maltose or cellobiose are used as the carbon source, not only the yield of 90% or more of xylitol is produced, but also of the xylose when glucose is used as the carbon source. It was found that the utilization rate of xylose increased rather than the utilization rate (28%). In particular, when glycerol is used as the carbon source, the production yield of xylitol of 100% and the utilization of xylose of 90% or more were found, and thus it was found to be most suitable for the production of xylitol.

Example 4 Preparation of Xylitol Using Glycerol as a Carbon Source (I)

First, the transformant BS-xdh prepared in Example 1 was inoculated in 3 ml of YM medium, incubated for 12 hours while shaking at 200 rpm at 30 ° C., and then 1 ml of the electric culture was returned to 50 ml of YM medium. Inoculation was incubated for 12 hours with shaking at 30 ° C. at 200 rpm.

Subsequently, 50 ml of the culture medium was inoculated into a fermentor containing 1.0 l of a production medium containing 20 g / L of glycerol, incubated for 24 hours with stirring at 600 rpm at 30 ° C., followed by dry cell concentration over time, Changes in glucose concentration, glycerol concentration, xylose concentration and xylitol concentration were measured (see FIG. 2). At this time, the concentration of dry cells was measured by the method of Example 2, the concentration of glucose, glycerol, xylose and xylitol was measured using the HPLC system of Example 2.

Figure 2 is a graph showing the change in dry cell concentration, glucose concentration, glycerol concentration, xylose concentration and xylitol concentration over time when glycerol is produced using glycerol as a carbon source, (■) is a dry cell concentration Indicates a glucose concentration, (o) indicates a glycerol concentration, (o) indicates a xylose concentration, and (o) indicates a xylitol concentration. As shown in Figure 2, when the concentration of the cells at the beginning of the culture, the concentration of glucose was rapidly reduced, but the concentration of glycerol was not significantly reduced, it was found that glucose affects the growth of the cells. In addition, the concentration of glycerol was also drastically decreased and the concentration of xylitol was rapidly increased in the section in which the concentration of xylose was rapidly decreased, indicating that glycerol had no effect on the growth of the cells and had an effect on the production of xylitol. there was. In addition, the production of xylitol was terminated within 15 hours after the start of the culture, wherein the productivity of xylitol was 2.97 g / L / h and the yield was 93.7%.

Example 5 Preparation of Xylitol Using Glycerol as a Carbon Source (II)

First, the transformant BS-xdh prepared in Example 1 was inoculated in 3 ml of YM medium, and incubated for 12 hours while shaking at 200 rpm at 30 ° C.

Subsequently, 1 ml of the culture was inoculated into 50 ml of a production medium containing 10 g / L of glycerol, and cultured for 60 hours while shaking at 200 rpm at 30 ° C. While incubating, samples (samples 11 to 18) were obtained at the time points 0, 6, 12, 18, 24, 36, 48 and 60 hours elapsed, and the dry cell concentration, glycerol concentration, xylose concentration and xylitol concentration. Was measured (see Table 3). At this time, the concentration of dry cells was measured by the method of Example 2, the concentration of glycerol, xylose and xylitol was measured using the HPLC system of Example 2.

Changes in Dry Cell Concentration, Glycerol, Xylose and Xylitol Concentrations over Time in Medium Using Glycerol as a Carbon Source sample Incubation time (h) Dry cell concentration (g / L) Glycerol Concentration (g / L) Xylose Concentration (g / L) Xylitol Concentration (g / L) 11 0 0.32 9.69 47.43 0.00 12 6 1.85 9.57 47.37 0.00 13 12 6.89 8.73 40.21 7.40 14 18 6.72 7.63 29.53 15.12 15 24 6.82 5.84 21.20 27.71 16 36 6.57 2.09 3.05 41.49 17 48 6.57 2.10 0 46.61 18 60 6.62 2.11 0 46.21

As shown in Table 3, it was found that after 48 hours of incubation, all of the xylose in the medium was converted to xylitol, and it was confirmed that the product yielded 2.97 g / L / h and yield of 93.7%. This was confirmed that the yield is much higher than the 80% yield of xylitol using the conventional Candida Tropicalis disclosed in the Republic of Korea Patent Registration No. 199819.

As described and demonstrated in detail above, the present invention provides a method for producing xylitol in high yield using a xylitol producing strain in which the expression of xylitol dehydrogenase is suppressed. When the high yield production method of xylitol of the present invention is used, xylitol can be produced in a higher yield than the conventional production method, and thus it can be widely used in the manufacture of various foods, medicines and the like including xylitol.

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Claims (7)

Xylitol-producing strains from which the xylitol dehydrogenase activity is completely removed from the xylitol dehydrogenase gene are removed. Inoculating the containing medium, culturing until the entire amount of xylose contained in the medium, and then obtaining the xylitol therefrom, comprising a high yield production method of xylitol. The method of claim 1, Xylitol producing strain is characterized in that the strain of the genus Candida High yield production method of xylitol. The method of claim 2, Candida sp is characterized in that Candida obtain the boiler Mondi (C. guillermondi), Candida parapsilosis (C. parapsilosis) or Candida Tropical faecalis (C. tropicalis) High yield production method of xylitol. delete The method of claim 1, Nitrogen source is characterized in that the yeast extract High yield production method of xylitol. The method of claim 1, Trace elements are characterized in that potassium diphosphate, magnesium sulfate or mixtures thereof High yield production method of xylitol. The method of claim 1, Xylitol producing strain is characterized in that the culture at 20 to 40 ℃ High yield production method of xylitol.

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