Aureobasidium pullulans, application thereof and method for producing medium-molecular-weight pullulan

By screening and identifying the high-vibrant budding terrium strain SYCY-018 and optimizing the fermentation conditions, the problems of low yield of prilantosaccharides and intolerance to high temperatures in the prior art were solved, and the high yield and genetic stability of medium molecular weight prolantosaccharides were achieved.

CN120118756AActive Publication Date: 2025-06-10BINZHOU SANYUAN BIOLOGICAL TECH

Patent Information

Application Number
CN202510584906.0
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-05-08
Publication Date
2025-06-10
Estimated Expiration
2045-05-08

AI Technical Summary

Technical Problem

The existing budding terrium strains used for fermentation and production of Prulandosugar are low in viability, insufficient yield, and intolerant to high temperatures, and their genetic stability has not been fully verified.

Method used

The high-vibrant budding terrium strain SYCY-018 was screened and identified. This strain has high genetic stability and temperature resistance. By optimizing fermentation conditions (such as temperature, pH, rotation speed, sucrose supplementation, etc.), the yield and molecular weight of plulandosaccharides were improved.

Benefits of technology

It has achieved high yield of medium molecular weight Plulandosaccharide, with a yield of up to 150 g/L, with good temperature stability and genetic stability, and is suitable for industrial production.

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Abstract

The invention discloses aureobasidium pullulans, application thereof and a method for producing medium-molecular-weight pullulan, and belongs to the technical field of microorganisms. The aureobasidium pullulans disclosed by the invention is aureobasidium pullulans SYCY-018, the strain is preserved in the general microbiological center of the China Committee for Culture Collection of Microorganisms on December 26, 2022, and the preservation number is CGMCC (China General Microbiological Culture Collection Center) NO.40467. According to the aureobasidium pullulans SYCY-018, the aureobasidium pullulans SYCY-018 and the aureobasidium pullulans The aureobasidium pullulans SYCY-018 is inoculated into a fermentation medium for fermentation to produce the pullulan, the yield of the medium-molecular-weight pullulan reaches up to 150 g / L or above, meanwhile, good hereditary stability and high temperature resistance are achieved, the yield of the pullulan can still be higher than 130 g / L even at the high temperature of 40 DEG C, and the aureobasidium pullulans SYCY-018 is suitable for industrial production.
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Description

Technical Field

[0001] The present invention relates to the field of microbial technology, and in particular, to Aureobasidium pullulans, its application, and a method for producing medium-molecular-weight pullulan polysaccharide. Background Art

[0002] The information disclosed in the background art of the present invention is only intended to increase the understanding of the overall background of the present invention, and is not necessarily regarded as an admission or an indication in any form that this information constitutes the prior art already known to those of ordinary skill in the art.

[0003] Pullulan polysaccharide, also known as pullulan or aureobasidin, is an important metabolite of Aureobasidium pullulans; it is a colorless, odorless, tasteless, non-toxic, edible polymer substance with good safety, heat resistance, solubility, salt and acid-base resistance, adhesiveness, strong plasticity, natural degradability, and good film-forming properties. Pullulan polysaccharide is composed of maltotriose as the basic unit, which is repeatedly connected by α-(1→6) glycosidic bonds. The unique connection method endows it with unique physical and chemical properties, so it is widely used in various fields of medicine and food.

[0004] The molecular weight of pullulan polysaccharide is not fixed, generally between 5.0×10 4 ~5.0×10 6 Da, and the degree of polymerization is generally in the range of 100-5000. The molecular weight and degree of polymerization are closely related to the type of strain and fermentation conditions. Medium-molecular-weight (2.0×10 5 ~1.0×10 6 Da) pullulan polysaccharide has good market prospects in the fields of capsule application and food preservation.

[0005] Currently, the vitality of Aureobasidium pullulans strains used for fermentative production of pullulan polysaccharide is generally low. For example, in patents CN115141757A and CN114381381A, the yield of pullulan polysaccharide is less than 100 g / L. The patent with the authorization publication number CN115197857B discloses an Aureobasidium pullulans that can improve the yield of pullulan polysaccharide and produce medium-molecular-weight pullulan polysaccharide, which is a recombinant bacterium obtained by knocking out or weakening the poly(malic acid) synthase gene in the metabolic pathway of Aureobasidium pullulans with the preservation number CGMCC NO. 23807. After 120 h of fermentation, the yield of pullulan polysaccharide of this strain can reach 129.1 g / L. Although its yield is about 50% higher than that of the original strain, it is still relatively low. In addition, the fermentation temperature of this strain is 28±2°C, which is likely to have a significant impact on the yield of pullulan polysaccharide when the summer temperature is high; moreover, the genetic stability of this recombinant bacterium is not disclosed in this patent.

[0006] Therefore, it is an urgent problem to be solved to provide a Aureobasidium pullulans with high production of medium and high molecular weight pullulan polysaccharide, good temperature tolerance and genetic stability. Summary of the Invention

[0007] In view of this, the present invention provides an Aureobasidium pullulans, its application and a method for producing medium molecular weight pullulan polysaccharide. Using the Aureobasidium pullulans of the present invention to produce pullulan polysaccharide, the yield of pullulan polysaccharide in the fermenter can be as high as more than 150 g / L, and it has good temperature tolerance and genetic stability.

[0008] In the first aspect, the present invention provides an Aureobasidium pullulans, which is Aureobasidium pullulans ( Aureobasidium pullulans ) SYCY-018. This strain was deposited in the General Microbiology Center of the China Committee for Culture Collection of Microorganisms on December 26, 2022, with the deposit number CGMCC NO. 40467.

[0009] The Aureobasidium pullulans SYCY-018 provided by the present invention is a highly viable strain screened from a corn farmland in Zhanhua, Binzhou, Shandong. It belongs to Aureobasidium pullulans through morphological and molecular biological identification.

[0010] In the second aspect, the present invention provides the application of the above-mentioned Aureobasidium pullulans, and the application is the application in the production of medium molecular weight pullulan polysaccharide.

[0011] In the third aspect, the present invention provides a method for producing medium molecular weight pullulan polysaccharide, and the method includes: Inoculating the above-mentioned Aureobasidium pullulans SYCY-018 on a YPD solid medium for activation culture, and then inoculating the activated cells into a YPD liquid medium for scale-up culture to obtain a seed solution; inoculating the seed solution into a fermentation medium for fermentation culture to obtain a fermentation broth, and purifying to obtain medium molecular weight pullulan polysaccharide.

[0012] Preferably, the temperature of the fermentation culture is 28-35 °C, the time of the fermentation culture is 100-120 h; the inoculation amount of inoculating the seed solution into the fermentation medium is 4-10% (v / v).

[0013] Preferably, the rotation speed during the fermentation culture process is 400-600 rpm, the pH is 6.0-8.0, and the dissolved oxygen is controlled at 30-40%.

[0014] Preferably, the composition of the fermentation medium is as follows: sucrose 100 - 130 g / L, yeast extract powder 3 - 6 g / L, ammonium sulfate 0.5 - 2 g / L, dipotassium hydrogen phosphate 3 - 6 g / L, magnesium sulfate heptahydrate 0.3 - 0.6 g / L, sodium chloride 0.5 - 2 g / L, and the solvent is water; during the fermentation process, a sucrose solution is added to make the total sucrose content in the medium 140 - 170 g / L.

[0015] Preferably, the temperature for the activation culture is 28 - 35 °C, and the time is 65 - 72 h.

[0016] Preferably, the temperature for the subculture is 28 - 35 °C, and the time is 32 - 48 h.

[0017] Furthermore, the specific process of the subculture is as follows: inoculate the activated bacterial cells into a test tube containing YPD liquid medium, culture at 28 - 35 °C and 180 - 250 rpm for 16 - 24 h, then transfer to a flask containing YPD liquid medium and culture at 28 - 35 °C and 180 - 250 rpm for 16 - 24 h to obtain a seed solution.

[0018] Preferably, the purification steps are as follows: centrifuge the fermentation broth, collect the supernatant, add ethanol and let it stand for precipitation, dry the obtained precipitate after centrifugation, and medium - molecular - weight pullulan polysaccharide is obtained.

[0019] Compared with the prior art, the present invention has achieved the following beneficial effects: (1) The Aureobasidium pullulans strain SYCY - 018 screened in the present invention has high vitality. Using it to produce pullulan polysaccharide, the yield of pullulan polysaccharide can be as high as over 150 g / L, with a high conversion rate, good genetic stability, and strong temperature stability. Even at a high temperature of 40 °C, the yield of pullulan polysaccharide is still higher than 130 g / L, which is suitable for industrial production.

[0020] (2) The average molecular weight of the pullulan polysaccharide produced by the Aureobasidium pullulans strain screened in the present invention is 5×10 5 ~8×10 5 Da, which has a broad market prospect in the production of medium - molecular - weight pullulan polysaccharide. Detailed Embodiments

[0021] It should be noted that the following detailed description is exemplary and is intended to provide further illustration of the present invention. Unless otherwise specified, all technical and scientific terms used herein have the same meaning as commonly understood by those of ordinary skill in the technical field to which the present invention belongs.

[0022] The technical solution of the present invention will be further described below in conjunction with specific embodiments. Unless otherwise specified, the present invention has no special restrictions on the sources of the reagents used in the following embodiments, and commercially available products well-known to those skilled in the art can be used.

[0023] In the following embodiments, the specific media used are as follows: (1)The composition of the YPD solid medium is as follows: glucose 20 g / L, peptone 20 g / L, yeast extract 10 g / L, agar 20 g / L, the solvent is water, and the pH is 7.0.

[0024] (2)The composition of the YPD liquid medium is as follows: glucose 20 g / L, peptone 20 g / L, yeast extract 10 g / L, the solvent is water, and the pH is 7.0.

[0025] (3)The composition of the fermentation medium is as follows: sucrose 120 g / L, yeast extract powder 5 g / L, ammonium sulfate 1 g / L, dipotassium hydrogen phosphate 5 g / L, magnesium sulfate heptahydrate 0.5 g / L, sodium chloride 1 g / L, the solvent is water, and the pH is 7.0.

[0026] Example 1 This example provides the screening of strains.

[0027] (1)Dilute the samples collected from the natural environment with sterile water, take part of the diluted solution and spread it on the YPD solid medium, culture at 30 °C for 70 h, observe the growth of colonies, screen out the strains with obvious drawing effect according to the colony morphology, color, and colony drawing situation, pick them with a sterile toothpick and streak culture on a new YPD solid medium, culture at 30 °C for 70 h, after the colonies grow, pick them out with a sterile toothpick and inoculate them into a 24-well deep well plate containing the fermentation medium, the liquid loading volume in each well is 2 mL, and culture at 30 °C and a rotation speed of 250 rpm for 110 h to obtain the fermentation broth.

[0028] (2)Centrifuge the fermentation broth in step (1), transfer the supernatant to a new 15 mL centrifuge tube (the centrifuge tube is weighed in advance), slowly add 2 times of absolute ethanol, let it stand for 8 h for precipitation, centrifuge again, place the obtained precipitate in an oven and dry it for 24 h, weigh it, and subtract the weight of the empty centrifuge tube to obtain the mass of pullulan polysaccharide, and further obtain the yield of pullulan polysaccharide.

[0029] A total of more than 2,600 strains were screened from more than 120 samples. Finally, a high-vitality Aureobasidium pullulans strain was screened from the corn farmland in Zhanhua, Binzhou, Shandong. This strain was named Aureobasidium pullulans ( Aureobasidium pullulansSYCY-018 was deposited at the General Microbiological Center of the China Committee for Culture Collection of Microorganisms on December 26, 2022, with the deposit number of CGMCC NO. 40467.

[0030] Example 2 This example provides a method for producing pullulan using Aureobasidium pullulans SYCY-018 screened in Example 1.

[0031] (1) Activation culture: Streak inoculate the Aureobasidium pullulans SYCY-018 strain on YPD solid medium and culture at 30 °C for 72 h to obtain the activated Aureobasidium pullulans strain.

[0032] (2) Subculture: Pick the activated Aureobasidium pullulans in step (1) and inoculate it into a test tube containing YPD liquid medium. Culture at 30 °C and 200 rpm for 20 h, then transfer it to a shake flask containing YPD medium and culture at 30 °C and 200 rpm for 20 h to obtain the seed liquid.

[0033] (3) Fermentation culture: Inoculate the seed liquid obtained in step (2) into the fermentation medium (250 L fermenter) with an inoculation amount of 5% (v / v). Set the fermentation temperature at 30 °C and the rotation speed at 500 rpm. Control the fermentation pH = 7.0 in the first 48 h of fermentation, then control the fermentation pH = 6.0. Control the dissolved oxygen throughout the fermentation at about 35%. Ferment for 110 h, and add sucrose solution during the fermentation process with a total addition amount of 50 g / L. End the fermentation when there is no sugar residue in the fermentation broth. After detection, the pullulan yield is 154.5 g / L.

[0034] (4) Extraction of pullulan: Centrifuge the fermentation broth after the fermentation in step (3) to remove the cells. Take the supernatant of the fermentation broth, slowly add 2 times the volume of absolute ethanol, let it stand for 8 h for precipitation, centrifuge again, and place the obtained white precipitate in an oven and dry it for 36 h to obtain pullulan.

[0035] (5) Determination of the molecular weight of pullulan: Determine it by high performance gel filtration chromatography (HPGFC). Instrument: Waters 2695 high performance liquid chromatograph (equipped with a 2410 refractive index detector and an Empower workstation). The chromatographic column used is: Ultrahydrogel Linear 300mm×7.8mm, the mobile phase is 0.1 M sodium nitrate, the flow rate is 0.5 mL / min, and the column temperature is controlled at 40 °C. Sample treatment: Weigh 20 mg of the dried sample, dissolve it with the mobile phase and make up the volume to 10 mL, and the injection volume is 10 μL. The weight average molecular weight (M w ) of the pullulan in step (4) is 7.2×105 Da。

[0036] Example 3 This example provides a genetic stability test for Aureobasidium pullulans SYCY-018 screened in Example 1.

[0037] Streak the Aureobasidium pullulans SYCY-018 strain on YPD solid medium to obtain the first-generation strain. According to this method, continue to streak the first-generation strain to obtain the second-generation strain, and so on to obtain the third, fourth, fifth, sixth, seventh, and eighth-generation strains. Activate each generation of strains, and the activation process is the same as in Example 2. Then inoculate them into the fermentation medium (5 L fermenter) respectively. Set the fermentation temperature at 30 °C, the rotation speed at 500 rpm. In the first 48 h of fermentation, control the fermentation pH at 7.0, and after 48 h, then control the fermentation pH at 6.0. The dissolved oxygen is controlled at about 35% during the whole fermentation process. Ferment for 110 h, and add sucrose solution during the fermentation process, with a total addition amount of 50 g / L. End the fermentation when there is no sugar residue in the fermentation broth. Detect the content of pullulan polysaccharide after fermentation. The detection results are shown in Table 1.

[0038] Table 1 Yield and molecular weight of pullulan polysaccharide of strains of different generations

[0039] It can be seen from Table 1 that with the increase of the number of passages, the yield of pullulan polysaccharide is relatively stable, indicating that the Aureobasidium pullulans SYCY-018 has good genetic stability.

[0040] Example 4 This example provides a verification of the high-temperature resistance of Aureobasidium pullulans SYCY-018 screened in Example 1.

[0041] In the process of industrial production, the temperature is difficult to accurately control, and there are also problems such as difficulty in cooling in summer. To further verify the high-temperature resistance performance of Aureobasidium pullulans SYCY-018, control the fermentation temperature at 30 - 40 °C and measure the yield of pullulan polysaccharide.

[0042] The activation and scale-up culture process refer to Example 2. Inoculate the seed liquid into the fermentation medium (5 L fermenter), with an inoculation amount of 5% (v / v). Set the fermentation temperatures at 30 °C / 35 °C / 40 °C respectively, the rotation speed at 500 rpm. In the first 48 h of fermentation, control the fermentation pH at 7.0, then control the fermentation pH at 6.0. The dissolved oxygen is controlled at about 35%. Ferment for 110 h, and add sucrose solution during the fermentation process, with a total addition amount of 50 g / L. End the fermentation when there is no sugar residue in the fermentation broth. Measure the yield of pullulan polysaccharide after fermentation. The detection results are shown in Table 2.

[0043] Table 2 Acid resistance test results of strains

[0044] Judging from the detection results, when the fermentation temperature is increased to 40 °C, the pullulan polysaccharide yield can also be maintained at 137.6 g / L, indicating that Aureobasidium pullulans strain SYCY-018 has good temperature stability.

[0045] The above are only the preferred embodiments of the present invention and are not intended to limit the present invention. For those skilled in the art, the present invention can have various changes and modifications. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.

Claims

1. A budding Aureobasidium pullulans, characterized in that: The budding Aureobasidium is Aureobasidium ( Aureobasidium pullulans )SYCY-018, the strain was deposited in the General Microbiology Center of China Microbiological Culture Collection Administration on December 26, 2022, with the deposit number CGMCC NO. 40467.

2. The use of Aureobasidium pullulans as claimed in claim 1, characterized in that: The application is the application in the production of medium molecular weight pullulan.

3. A method for producing medium molecular weight pullulan, characterized in that: The method comprises: The budding Aureobasidium pullulans SYCY-018 described in claim 1 is inoculated into a YPD solid culture medium for activation culture, and then the activated bacteria are inoculated into a YPD liquid culture medium for expansion culture to obtain a seed solution; the seed solution is inoculated into a fermentation medium for fermentation culture to obtain a fermentation solution, and the medium molecular weight pullulan is obtained through purification.

4. The method according to claim 3, characterized in that The fermentation culture temperature is 28-35° C., and the fermentation culture time is 100-120 h. The inoculation amount of the seed liquid inoculated into the fermentation medium is 4-10% (v / v).

5. The method according to claim 3, characterized in that The rotation speed of the fermentation culture process is 400-600 rpm, the pH is 6.0-8.0, and the dissolved oxygen is controlled at 30-40%.

6. The method according to claim 3, characterized in that The fermentation medium comprises: 100-130 g / L sucrose, 3-6 g / L yeast extract powder, 0.5-2 g / L ammonium sulfate, 3-6 g / L dipotassium hydrogen phosphate, 0.3-0.6 g / L magnesium sulfate heptahydrate, 0.5-2 g / L sodium chloride, and water as solvent; sucrose solution is added during the fermentation process to make the total sucrose content in the medium 140-170 g / L.

7. The method according to claim 3, characterized in that The activation culture is carried out at a temperature of 28-35° C. and for a time of 65-72 h.

8. The method according to claim 3, characterized in that The temperature of the expanded culture is 28-35°C and the time is 32-48 h.

9. The method according to claim 8, characterized in that The process of the expanded culture is specifically as follows: inoculating the activated bacteria into a test tube containing a YPD liquid culture medium, culturing for 16 to 24 hours at 28 to 35° C. and 180 to 250 rpm, and then transferring to a shake flask containing a YPD liquid culture medium, culturing for 16 to 24 hours at 28 to 35° C. and 180 to 250 rpm to obtain a seed solution.

10. The method according to claim 3, characterized in that The purification steps are: centrifuging the fermentation liquid, collecting the supernatant, adding ethanol and allowing to settle, and drying the obtained precipitate after centrifugation to obtain the medium molecular weight pullulan.

Citation Information

Patent Citations

  • Construction and application of aureobasidium pullulans for producing pullulan

    CN114381381A

  • A method for producing medium molecular weight pullulan polysaccharide using *Bacillus buddingus*

    CN115197857B

  • Fermentation method for producing pullulan polysaccharide

    CN101215592A

  • Method for increasing pulullan yield

    CN103695500A

  • Mutant strain capable of realizing high-efficiency production of low-molecular pulullan and application thereof

    CN107760608A

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