JP2000093188A - Fermentation for production of xylitol using candida tropicalis - Google Patents

Abstract

PROBLEM TO BE SOLVED: To produce xylitol in high productivity and yield by fermenting new Candida tropicalis strain at respectively specific pH, temperature and dissolved oxygen concentration in a medium having a specific composition to give maximum productivity of xylitol. SOLUTION: Xylitol is produced at maximized productivity by using a new Candida tropicalis strain deposited under KCCM-10122 at the Korean Microorganism Culture Center as the fermentation microorganism, fermenting a xylose culture medium having a composition to give maximum productivity of xylitol, i.e., 5-20 w/v% xylose, 0.2-1.0 w/v% glucose, 0.2-2.0 w/v% yeast extract, 0.2-2.0 w/v% ammonium sulfate, 0.2-2.0 w/v% KH2PO4 and 0.01-0.2 w/v% MgSO4.7H2O at pH 4.5-5.5 and 27-33 deg.C at a air saturation ratio of 0.1-5.0% in terms of dissolved oxygen concentration in the medium while controlling the reduction- oxidation potential in the culture base to -50 to -150 mV, removing cells and other residues from the fermentation product and recovering the objective product from the culture base.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

The present invention relates to a fermentation method for producing xylitol with high productivity and high yield by using a novel strain of Candida tropicalis, and more particularly, to a culture medium containing xylose. And the pH, temperature and D
The present invention relates to a fermentation process for producing xylitol under optimal fermentation conditions to produce maximum amounts of xylitol by optimizing environmental conditions such as O concentration.

[0002]

2. Description of the Related Art Xylitol (xylo-pentane-1,
2,3,4,5 pentol) is a naturally occurring 5-carbon sugar alcohol that is present in small amounts in various fruits, vegetables, and mushrooms. It can be produced by treating plants such as jute branches and beech wood residues with oxalic acid. However, compared to the amount of sugarcane and sugar beet, only small amounts present in natural resources
Its quantitative extraction is difficult and uneconomical. In addition, xylitol is a standard metabolic intermediate in carbohydrate metabolism in mammals. Xylitol has a number of advantageous natural properties. Xylitol has antipyretic properties to prevent acid formation, and can promote and prevent oral hygiene. Since xylitol does not require insulin to regulate its metabolic effects, it can also be used to treat diabetes as a sugar substitute. Xylitol is also an ideal sweetener for those who are deficient in glucose-6-phosphate dehydrogenase, since its metabolism does not involve glucose-6-phosphate dehydrogenase.

On an industrial scale, xylitol is produced by the chemical reduction of xylose derived from birchwood or a hemicellulose hydrolyzate rich in xylose. Since the hemicellulose fraction of these feedstocks contains polymers of other sugars, this processing step involves extensive purification and isolation steps to remove by-products from xylose or xylitol. The yield of xylitol is about 50-60%. Therefore, xylitol is an expensive product. The production of xylitol by chemical methods was known to be expensive due to the difficulty of its isolation and purification steps, so explore alternative ways to produce xylitol effectively using microorganisms Doing is worthwhile.

[0004] To overcome the above disadvantages of chemical manufacturing processes, biological fermentation processes for xylitol production have been studied.
A fermentation process for producing xylitol using yeast species from a culture medium containing xylose or a hemicellulose hydrolyzate having xylose is disclosed. In particular, Candida blankii (Candida blankii),
Candida Guillermondi (Candida guide)
liermondii), Candida tropicalis (Ca)
ndida tropicalis, Candida utilis, Saccharomyces bail
ii), Saccharomyces roxii (Sacchar)
omyces rouxii), Saccharomyces uvariu
m), and Saccharomyces pombe (Sacchar
Omyces pombe) is known as a microorganism that produces xylitol. However, the production of xylitol is less desirable because of its slow production rate.

[0005] To improve xylitol yield and productivity, the high xylitol producing yeast of the present invention was isolated from sludge of a xylose manufacturing plant and identified as Candida tropicalis. Fermentation conditions are optimized using this strain to produce the maximum amount of xylitol.

[0006]

SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing xylitol with a high productivity and a high yield under the Budapest Treaty on February 20, 1998 under the accession number KCCM-10122. Center (Korean Culture Center)
er) and Candida tropicalis (Candi)
(D. tropicalis) of the present invention.

Another object of the present invention is to provide: i) the following fermentation conditions: a) xylose having a composition of a culture medium for obtaining maximum production of xylitol of 5 to 20 (w / v)%; .
0 (w / v)% glucose, 0.2-2.0 (w / v)
% Yeast extract, 0.2-2.0 (w / v)% (N
_{H 4) 2 SO 4, 0.2~2.0} (w / v)% of KH ₂ PO ₄
And 0.01~0.2 (w / v)% of MgSO ₄ · 7H ₂
B) pH of the culture medium is 4.5-5.5; c) Culture temperature is 27-33 ° C. d) The dissolved oxygen concentration in the culture medium is 0.1 to 5.0 (w /
v)% air saturation; and e) the redox (reduction-oxidation) potential in the culture medium is-
Culturing xylose media in the pores by controlling: ii) removing cells and other residues from the fermentation media; iii) removing xylitol from the fermentation media in step ii) above. Isolation and recovery; accession number KCC consisting of steps
Candida trophos (Candida trophis) deposited at Korean Culture Center with M-10122
The present invention is to provide an optimal fermentation method for maximizing xylitol production using a novel strain of P. picalis.

It is a further object of the present invention to provide a method wherein xylose and glucose are provided during the xylitol production phase by: i) providing xylose intermittently to the liquid medium; and / or ii) continuously providing xylose and glucose. 20: 1 ~
Providing a 5: 1 (w / w) mixture; to provide a fermentation process that is fed to the culture medium.

[0009]

SUMMARY OF THE INVENTION The present invention relates to a xylose manufacturing plant (Korea Biotech Co., Ltd. [Korea Biot]).
ech Co. ], Candida tropicalis isolated from sludge in Anyang City, Korea
For obtaining xylitol in high yield and high volumetric productivity. The cells used in the present invention are isolated by the following method.

[0010] The liquid medium of the sludge used in the production of xylose is 0.8 to 1.2% glucose, 0.4 to 0.6%.
On a yeast-malt (YM) plate containing 0.3 to 0.5% yeast extract and 0.2 to 0.4% malt extract and 1.2 to 1.8% agar. , 28 to 3
Incubate at a temperature of 2 ° C. Some of the colonies are selected as fast growing strains. 5-15% of selected colonies
Xylose, 0.2-0.8% yeast extract, 0.2%
2 to 0.8% of (NH _{4) 2} SO ₄ and from 0.2 to 0.8% of KH ₂ PO ₄ was transferred onto the fermentation culture medium containing, for testing the production activity of xylitol in shake flasks. 28-32
24 ° C. at a temperature of 200 ° C. and a rotation speed of 200 to 240 rpm.
After ３６36 hours of culture, high xylitol producing strains are selected. Many strains isolated from sludge for producing xylose can be obtained by repeating the above selection method 10 times or more. Finally, the highest xylitol-producing colonies are isolated and used as xylitol-producing strains in the present invention.

A discussion of the morphological, cultural, and physiological properties is based on the Kreger-Vanridge method [Kreger-V.
an Rij method] (yeast: taxonomic study Ervier Science Publisher, Amsterdam, 1984) [The yeasts: a taxo
nomic study Elevator Science
e Publisher, Amsterdam, 198
4], and the isolated strain was isolated by the Barnett method (yeast: characteristics and identification; Cambridge University Newspaper, London, 198).
3) [Yeasts: Characteristic]
s and Identification. Cambr
idge University Press, Lon
don, 1983]. The physiological characteristics of the isolated strain are as follows.

I) Growth temperature 20 ° C. + 30 ° C. + 37 ° C. + 42 ° C.-ii) Growth + 30% D-glucose + 40% D-glucose + iii) Urea hydrolysis-iv) Starch formation -v ) Formation reaction of diazonium blue B-vi) assimilation of nitrate-vii) release of arbutin-viii) assimilation of filament + ix) assimilation of carbon source glucose + galactose + L-sorbose-sucrose + maltose + lactose-trehalose + cellobiose-melibiose -Raffinose + melesitose-soluble starch + D-xylose + L-arabinose + D-arabinose-D-ribose- D-rhamnose-glycerol + erythritol-ribitol + galactitol-D- mannitol + D- sorbitol + D-glu Tall - Xylitol - inositol - salicin - inulin - DL-lactic acid - succinic acid + citric acid + formic acid - ethanol + methanol -

[0013] From these results, the isolated strain is Candida tropicalis.
s). These cells have the accession number KCCM
Korean microorganism culture (Korean)
Culture). The following is a description of a fermentation method for producing xylitol using cells as described above.

Seed culture Candida tropicalis (Candida tropical)
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask. The seed culture is then transferred to a 5 L fermentor for producing xylitol in the main culture.

Main culture The fermentation culture medium contains 5 to 20 (w / v)% xylose,
0.2-2.0 (w / v)% yeast extract, 0.2-2.0 (w / v)
2.0 (w / v)% glucose, 0.2-2.0 (w / v)
v)% of _{(NH 4) 2 SO 4,} 0.2~2.0 (w / v)%
KH ₂ PO ₄ , and 0.01-0.2 (w / v)% M
gSO composed of ₄ · 7H ₂ O. Fed-batch cultivation in a fermenter containing a fermentation medium is carried out at a temperature of 28-32 ° C. and a pH of 4.5-5.5. Stirring speed 300 ~
It is 600 rpm. In the xylitol production stage,
The dissolved oxygen concentration in the culture medium is air saturation of 0.1-5.0%, and the redox (reduction-oxidation) potential in the culture medium is -50 to -150 mV, preferably -80 to 50 mV.
-120 mV. Fed-batch cultivation is performed using 2 L of initial culture medium and the final volume is brought to 3 L by feeding 1.0 L of a mixed solution of xylose and glucose.

[0016] The fermentation treatment is preferably carried out by a fed-batch method. After xylose was completely consumed in the medium, the amounts of xylitol, glucose and xylitol were measured on a Sugar-Pak I column (Sugar-
It is measured using high performance liquid chromatography equipped with a Pak I column. The dry cell weight is 60
It is estimated using a calibration curve obtained from the relationship between the optical density at 0 nm and the weight of the dried cells.

The measured xylitol yield is 85-98% of the biomass of xylose consumption, and the volumetric productivity is 3.0-7.0 g / L-hr, both conventional fermentation yield and It has increased by a factor of 5 to 15 compared to the productivity. Finally, the fermentation broth is centrifuged to remove cells and other residues, and the supernatant is filtered and dialyzed to obtain xylitol. The present invention can be described in more detail by the following examples, but the scope of the present invention is not limited thereto.

[0018]

EXAMPLES Example I Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract)
And seed culture in main culture
5 L of fermentation medium containing fermentation broth for producing toll
Transfer to fermenter. The initial fermentation culture medium is 5 to 15 (w /
v)% xylose, 0.2-1.5 (w / v)% e
Strike extract, 0.2-2.0 (w / v)% (NH_Four)_TwoS
O _Four, 0.2-2.0 (w / v)% KH_TwoPO_Four, 0.01
~ 0.2 (w / v)% MgSO_Four・ 7H_TwoComposed of O
You. The fed-batch cultivation in the fermenter is performed at 28-32 ° C.
It is carried out at a temperature and a pH of 4.5 to 5.5. The stirring speed is 3
It is 00-600 rpm. In the xylitol production stage
And the concentration of dissolved oxygen in the culture medium is 0.1 to 5.0%.
Gas saturation and redox (reduction) in the culture medium.
-Oxidation) potential is -50 to -150 mV, preferably -8
0 to -120 mV. The culture was completely free of xylose
Implemented until spent. Xylose fed-batch culture
Nutrition controls high xylose concentration in xylitol production
Implemented for production. The capacity of the fermenter is 150 g
To supply 250 ml containing xylose four times
Therefore (20, 27, 34, 41 hours), 200 g of key
Contains 2L to 900g xylose containing sylose
Increase to 3L.

After the fermentation for 48 hours, the amount of xylitol was measured using a Sugar-Pak I column.
column). 3
00 g / L xylose gives 240 g / L xylitol, which corresponds to 80% of the xylitol yield from xylose. The xylitol production rate of the intermittent fed-batch culture is 5.00 g / L-hr.

EXAMPLE II Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The fermentation medium is 5 to 15 (w / v)%
Xylose, 0.2-1.5 (w / v)% yeast extract, 0.2-2.0 (w / v)% (NH ₄ ) ₂ SO ₄ ,
0.2~2.0 (w / v)% of KH ₂ PO _4, 0.01~0.
Consists of 2 (w / v)% of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is performed at a temperature of 28-32 ° C and a pH of 4.5-5.5. Stirring speed 300 ~
It is 600 rpm. In the xylitol production stage,
The dissolved oxygen concentration in the culture medium is air saturation of 0.1-5.0%, and the redox (reduction-oxidation) potential in the culture medium is -50 to -150 mV, preferably -80 to 50 mV.
-120 mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter is increased from 2 L containing 900 g xylose by continuously feeding a 1 L solution containing 700 g xylose. The xylose feed is started at a residual xylose rate of 3.0-6.0%.

After the fermentation for 48 hours, the amount of xylitol was measured using a Sugar-Pak I column.
column). 3
00 g / L xylose yields 255 g / L xylitol, which corresponds to 85% of the xylitol yield from xylose. The xylitol production rate of the intermittent fed-batch culture is 5.31 g / L-hr.

EXAMPLE III Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The fermentation medium is 5 to 15 (w / v)%
Xylose, 0.5-2.0 (w / v)% glucose, 0.2-2.0 (w / v)% yeast extract, 0.5%
2~2.0 (w / v)% of _{(NH 4) 2 SO 4,} 0.2~2.
0 (w / v)% of _{KH 2 PO 4, 0.01~0.2 (w} /
v)% of consisting of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is performed at a temperature of 28-32 ° C and a pH of
Perform at 4.5-5.5. The stirring speed is 300-600r
pm. During the xylitol production stage, the dissolved oxygen concentration in the culture medium is between 0.1 and 5.0% air saturation, and the redox (reduction-oxidation) potential in the culture medium is between -50 and -150 mV, preferably-. 80 to -120
mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter is increased from 2 L containing 900 g xylose by continuously feeding a 1 L solution containing 700 g xylose and 35 g glucose. Xylose supply is 3.0-6.0
Starting at a percent xylose residual.

After fermentation for 48 hours, the amount of xylitol was measured using a Sugar-Pak I column.
column). 3
270 g / L xylitol was obtained from 00 g / L xylose, which corresponds to 90% of the xylitol yield from xylose. The xylitol production rate of a continuous fed-batch culture of xylose and glucose was 5.6.
3 g / L-hr.

EXAMPLE IV Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The fermentation medium is 5 to 15 (w / v)%
Xylose, 0.5-2.0 (w / v)% glucose, 0.2-2.0 (w / v)% yeast extract, 0.5%
2~2.0 (w / v)% of _{(NH 4) 2 SO 4,} 0.2~2.
0 (w / v)% of _{KH 2 PO 4, 0.01~0.2 (w} /
v)% of consisting of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is performed at a temperature of 28-32 ° C and a pH of
Perform at 4.5-5.5. The stirring speed is 300-600r
pm. During the xylitol production stage, the dissolved oxygen concentration in the culture medium is between 0.1 and 5.0% air saturation, and the redox (reduction-oxidation) potential in the culture medium is between -50 and -150 mV, preferably-. 80 to -120
mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter was increased from 2 L containing 900 g xylose to 700 g xylose and 100 g
The volume is increased by continuously feeding a 1 L solution containing glucose. The supply of xylose is 3.0-6.
It starts at a residual xylose rate of 0%.

After the fermentation for 48 hours, the amount of xylitol was measured using a Sugar-Pak I column.
column). 3
00 g / L xylose gives 290 g / L xylitol, which corresponds to 97% of the xylitol yield from xylose. The xylitol production rate of a continuous fed-batch culture of xylose and glucose was 6.0.
4 g / L-hr.

Example V Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The initial fermentation culture medium is 5 to 15 (w /
v)% xylose, 0.5-2.0 (w / v)% glucose, 0.2-1.5 (w / v)% yeast extract,
0.2-2.0 (w / v)% of (NH ₄ ) ₂ SO ₄ , 0.2-2.0
2.0 (w / v)% of KH ₂ PO _4, 0.01~0.2 (w
/ V)% of consisting of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is carried out at a temperature of 28-32 ° C and p
H4.5-5.5. The stirring speed is 300-600
rpm. During the xylitol production stage, the dissolved oxygen concentration in the culture medium is between 0.1 and 5.0% air saturation, and the redox (reduction-oxidation) potential in the culture medium is between -50 and -150 mV, preferably-. 80 to -120
mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter was increased from 2 L containing 900 g xylose to 700 g xylose and 140 g
The volume is increased by continuously feeding a 1 L solution containing glucose. The supply of xylose is 3.0-6.
It starts at a residual xylose rate of 0%.

After fermentation for 48 hours, the amount of xylitol was measured using a Sugar-Pak I column.
column). 3
00 g / L xylose yielded 280 g / L xylitol, which corresponds to 93% of the xylitol yield from xylose. The xylitol production rate of a continuous fed-batch culture of xylose and glucose was 5.8.
3 g / L-hr.

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[Procedure amendment]

[Submission date] October 18, 1999 (1999.10.
18)

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[0006]

SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing xylitol with a high productivity and a high yield under the Budapest Treaty on February 20, 1998 under the accession number KCCM-10122. Center (Korean Culture Center)
er) and Candida tropicalis (Candi)
da tropicalis) using a novel strain
It is to provide a fermentation method .

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It is an object of the present invention to: i) grow cells in YM medium at 28-32 ° C. for 8-16 hours;
Grown and cultivated, wherein the YM medium is 0.8-1.2.
(W / v)% glucose, 0.4-0.6 (w / v)%
Peptone, 0.3-0.5 (w / v)% yeast extraction
And 0.2 to 0.4 (w / v)% malt extract.
A; ii) following fermentation conditions; a) Composition of the culture medium for maximum production of xylitol 5~20 (w / v)% of xylose, 0.2.
0 (w / v)% glucose, 0.2-2.0 (w / v)
% Yeast extract, 0.2-2.0 (w / v)% (N
_{H 4) 2 SO 4, 0.2~2.0} (w / v)% of KH ₂ PO ₄
And 0.01~0.2 (w / v)% of MgSO ₄ · 7H ₂
B) pH of the culture medium is 4.5-5.5; c) Culture temperature is 28-32 ° C. d) The dissolved oxygen concentration in the culture medium is 0.1 to 5.0 (w /
v)% air saturation; and e) the redox (reduction-oxidation) potential in the culture medium is-
Xylose medium is fermented with the cells grown in step i) by controlling between 50 and -150 mV ; iii) xylose during the xylitol production phase of cell growth.
A mixture of glucose and glucose, where xylose and
The weight ratio of glucose 20: 1-5: be 1; iv) the cells and other residues were removed from the fermentation medium; and v) xylitol was isolated recovered from the fermentation medium of the step iv); Korean Culture Center with accession number KCCM-10122
It is an object of the present invention to provide a fed-batch fermentation method that is optimal for maximizing xylitol production using a novel strain of Candida tropicalis deposited with the C. ure Center.

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Main culture The fermentation culture medium contains 5 to 20 (w / v)% xylose,
0.2-2.0 (w / v)% yeast extract, 0.2-2.0 (w / v)
1.0 (w / v)% glucose, 0.2-2.0 (w / v)
v)% of _{(NH 4) 2 SO 4,} 0.2~2.0 (w / v)%
KH ₂ PO ₄ , and 0.01-0.2 (w / v)% M
gSO composed of ₄ · 7H ₂ O. Fed-batch cultivation in a fermenter containing a fermentation medium is carried out at a temperature of 28-32 ° C. and a pH of 4.5-5.5. Stirring speed 300 ~
It is 600 rpm. In the xylitol production stage,
The dissolved oxygen concentration in the culture medium is air saturation of 0.1-5.0%, and the redox (reduction-oxidation) potential in the culture medium is -50 to -150 mV, preferably -80 to 50 mV.
-120 mV. Fed-batch cultivation is performed using 2 L of initial culture medium and the final volume is brought to 3 L by feeding 1.0 L of a mixed solution of xylose and glucose. In this mixed solution, xylose and glue
The weight ratio of the course is from 20: 1 to 5: 1.

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[0022]

EXAMPLES Example I Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The fermentation medium is 5 to 15 (w / v)%
Xylose, 0.2-1.0 (w / v)% glucose, 0.2-2.0 (w / v)% yeast extract, 0.2%
2~2.0 (w / v)% of _{(NH 4) 2 SO 4,} 0.2~2.
0 (w / v)% of _{KH 2 PO 4, 0.01~0.2 (w} /
v)% of consisting of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is performed at a temperature of 28-32 ° C and a pH of
Perform at 4.5-5.5. The stirring speed is 300-600r
pm. During the xylitol production stage, the dissolved oxygen concentration in the culture medium is between 0.1 and 5.0% air saturation, and the redox (reduction-oxidation) potential in the culture medium is between -50 and -150 mV, preferably-. 80 to -120
mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter is increased from 2 L containing 900 g xylose by continuously feeding a 1 L solution containing 700 g xylose and 35 g glucose. Xylose supply is 3.0-6.0
Starting at a percent xylose residual.

[Procedure amendment 11]

[Document name to be amended] Statement

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[Correction method] Change

[Correction contents]

EXAMPLE II Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The fermentation medium is 5 to 15 (w / v)%
Xylose, 0.2-1.0 (w / v)% glucose, 0.2-2.0 (w / v)% yeast extract, 0.2%
2~2.0 (w / v)% of _{(NH 4) 2 SO 4,} 0.2~2.
0 (w / v)% of _{KH 2 PO 4, 0.01~0.2 (w} /
v)% of consisting of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is performed at a temperature of 28-32 ° C and a pH of
Perform at 4.5-5.5. The stirring speed is 300-600r
pm. During the xylitol production stage, the dissolved oxygen concentration in the culture medium is between 0.1 and 5.0% air saturation, and the redox (reduction-oxidation) potential in the culture medium is between -50 and -150 mV, preferably-. 80 to -120
mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter was increased from 2 L containing 900 g xylose to 700 g xylose and 100 g
The volume is increased by continuously feeding a 1 L solution containing glucose. The supply of xylose is 3.0-6.
It starts at a residual xylose rate of 0%.

[Procedure amendment 12]

[Document name to be amended] Statement

[Correction target item name] 0026

[Correction method] Change

[Correction contents]

EXAMPLE III Candida tropical
alis) (KCCM-10122) frozen (-70
C) cells at a temperature of 28-32C and 220-260.
40 to 60 ml of Y for 8 to 16 hours at a rotation speed of rpm
M medium (0.8-1.2 (w / v)% glucose,
0.4-0.6 (w / v)% peptone, 0.3-0.5
(W / v)% yeast extract and 0.2-0.4 (w
/ V)% malt extract) in a 250 ml flask and transfer the seed culture to a 5 L fermentor containing a fermentation medium for producing xylitol in the main culture. The initial fermentation culture medium is 5 to 15 (w /
v)% xylose, 0.2-1.0 (w / v)% glucose, 0.2-1.5 (w / v)% yeast extract,
0.2-2.0 (w / v)% of (NH ₄ ) ₂ SO ₄ , 0.2-2.0
2.0 (w / v)% of KH ₂ PO _4, 0.01~0.2 (w
/ V)% of consisting of MgSO ₄ · 7H ₂ O. The fed-batch cultivation in the fermenter is carried out at a temperature of 28-32 ° C and p
H4.5-5.5. The stirring speed is 300-600
rpm. During the xylitol production stage, the dissolved oxygen concentration in the culture medium is between 0.1 and 5.0% air saturation, and the redox (reduction-oxidation) potential in the culture medium is between -50 and -150 mV, preferably-. 80 to -120
mV. The culturing is performed until xylose is completely consumed. Fed-batch cultivation of xylose is performed because of the inhibitory effect of high xylose concentration on xylitol production. The capacity of the fermenter was increased from 2 L containing 900 g xylose to 700 g xylose and 140 g
The volume is increased by continuously feeding a 1 L solution containing glucose. The supply of xylose is 3.0-6.
It starts at a residual xylose rate of 0%.

──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. ⁷ Identification FI FI Theme Court ゛ (Reference) C12R 1:74) (72) Inventor Deok Khun Oh Korea −Dong, Bisable Apartment 16−505 (72) Inventor Soo Lung Jun Seoul, Songpagu, Chamsil Le Dong 86 Asia Sansukjeong Apartment 1-901 F-term (Reference) 4B064 AC05 CA06 CC04 CC06 CC07 CC09 CC12 CD09 DA07 DA10 4B065 AA75X AC14 AC16 BA22 BB15 CA07 CA41 CA44

Claims (5)

[Claims] 1. i) The following fermentation conditions: a) xylose having a composition of a culture medium for obtaining maximum production of xylitol of 5 to 20 (w / v)%, 0.2 to 1.
0 (w / v)% glucose, 0.2-2.0 (w / v)
% Yeast extract, 0.2-2.0 (w / v)% (N
_{H 4) 2 SO 4, 0.2~2.0} (w / v)% of KH ₂ PO ₄
And 0.01~0.2 (w / v)% of MgSO ₄ · 7H ₂
B) pH of the culture medium is 4.5-5.5; c) Culture temperature is 27-33 ° C. d) The dissolved oxygen concentration in the culture medium is 0.1 to 5.0 (w /
v)% air saturation; and e) the redox (reduction-oxidation) potential in the culture medium is-
Fermenting xylose medium with the cells by controlling 50-150 mV; ii) removing cells and other residues from the fermentation medium; and iii) removing xylitol from the fermentation medium in step ii) above. Isolation and recovery; accession number KCC consisting of steps
A fermentation method for maximizing xylitol production using a novel strain of Candida tropicalis deposited with the Korean Microbial Culture Center having M-10122. 2. The cells used for fermentation are frozen Candida tropicalis (KCCM-10122), 0.8 to 1.2.
(W / v)% glucose, 0.4-0.6 (w / v)%
27-33 ° C. in a YM medium containing 0.3-0.5 (w / v)% yeast extract and 0.2-0.4 (w / v)% malt extract. The fermentation method according to claim 1, which is adjusted by culturing at a temperature of 6 to 18 hours. 3. The method according to claim 1, wherein xylose and glucose are supplied during the xylitol production phase; i) supplying xylose intermittently to the liquid medium; and / or ii) continuously xylose and glucose 20: 1 to 1
2. The fermentation process of claim 1, wherein the mixture is supplied to the culture medium by supplying a 5: 1 (w / w) mixture. 4. Candida tropicalis (KCCM-10)
122) The novel cell. 5. i) Wild-type Candida tropicalis (K
CCM-10122) on a yeast-malt (YM) medium and culturing; ii) isolating the generated colonies at least 10 times on the YM medium; and iii) isolating the rapidly growing colonies; Consisting of Candida tropicalis (KCCM-10
122).