• Title/Summary/Keyword: recombinant fermentation

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Secretory Expression and Purification of the Recombinant Duck Interleukin-2 in Pichia pastoris

  • Du, Cuihong;Han, Long;Xiao, Anfeng;Cao, Minjie
    • Journal of Microbiology and Biotechnology
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    • v.21 no.12
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    • pp.1264-1269
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    • 2011
  • Interleukin-2 (IL-2) is a vital cytokine secreted by activated T lymphocytes, and plays an important role in the regulation of cellular functions and immunity of animals. In this study, the recombinant duck IL-2 (rduIL-2) was secretory expressed in Pichia pastoris (P. pastoris). The recombinant P. pastoris strain was cultured in shake flasks and then scaled up in a 5.0-l bioreactor. The result showed that the maximal fresh-cell-weight of 594.1 g/l and the maximal $OD_{600}$ of 408 were achieved in the bioreactor. The rduIL-2 was purified by two steps of purification procedures, and approximately 311 mg of rduIL-2/L fermentation supernatant was obtained. SDS-PAGE showed that the purified rduIL-2 constituted a homogeneous band of ~16 kDa or ~14 kDa corresponding to the glycosylated or non-glycosylated duIL-2 protein in size, respectively. The bioactivity of rduIL-2 was determined by lymphocyte proliferation assay. The result indicated that the rduIL-2 greatly promoted the proliferation of ConA-stimulated lymphocytes in vitro. The P. pastoris expression system described here could provide promising, inexpensive, and large-scale production of the rduIL-2, which lays the foundation for development of novel immunoadjuvants to enhance both the immunity of ducks against various infectious pathogens and vaccine efficacy.

Effect of Incorrectly Estimated Parameters on the Control of Specific Growth Rate in E. coli Fed-Batch Fermentation

  • Park, Tai-Hyun;Yoon, Sung-Kwan;Kang, Whan-Koo
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.1 no.1
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    • pp.22-25
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    • 1996
  • An Exponetial feeding strategy has been frequently used in fed-batch fermentation of recombinant E. coli. In this feeding scheme, growth yield and initial cell concentration, which can be erroneously determined, are needed to calculate the feed rate for controlling specific growth rate at the set point. The effect of the incorrect growth yield and initial cell concentration on the control of the specific growth rate was theoretically analyzed. Insignificance of the correctness of those parameters for the control of the specific growth rate was shown theoretically and experimentally.

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Production of Cellulosic Ethanol in Saccharomyces cerevisiae Heterologous Expressing Clostridium thermocellum Endoglucanase and Saccharomycopsis fibuligera β-glucosidase Genes

  • Jeon, Eugene;Hyeon, Jeong-eun;Suh, Dong Jin;Suh, Young-Woong;Kim, Seoung Wook;Song, Kwang Ho;Han, Sung Ok
    • Molecules and Cells
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    • v.28 no.4
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    • pp.369-373
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    • 2009
  • Heterologous secretory expression of endoglucanase E (Clostridium thermocellum) and ${\beta}$-glucosidase 1 (Saccharomycopsis fibuligera) was achieved in Saccharomyces cerevisiae fermentation cultures as an ${\alpha}$-mating factor signal peptide fusion, based on the native enzyme coding sequence. Ethanol production depends on simultaneous saccharification of cellulose to glucose and fermentation of glucose to ethanol by a recombinant yeast strain as a microbial biocatalyst. Recombinant yeast strain expressing endoglucanase and ${\beta}$-glucosidase was able to produce ethanol from ${\beta}$-glucan, CMC and acid swollen cellulose. This indicates that the resultant yeast strain of this study acts efficiently as a whole cell biocatalyst.

High ${\beta}$-Glucosidase Secretion in Saccharomyces cerevisiae Improves the Efficiency of Cellulase Hydrolysis and Ethanol Production in Simultaneous Saccharification and Fermentation

  • Tang, Hongting;Hou, Jin;Shen, Yu;Xu, Lili;Yang, Hui;Fang, Xu;Bao, Xiaoming
    • Journal of Microbiology and Biotechnology
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    • v.23 no.11
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    • pp.1577-1585
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    • 2013
  • Bioethanol production from lignocellulose is considered as a sustainable biofuel supply. However, the low cellulose hydrolysis efficiency limits the cellulosic ethanol production. The cellulase is strongly inhibited by the major end product cellobiose, which can be relieved by the addition of ${\beta}$-glucosidase. In this study, three ${\beta}$-glucosidases from different organisms were respectively expressed in Saccharomyces cerevisiae and the ${\beta}$-glucosidase from Saccharomycopsis fibuligera showed the best activity (5.2 U/ml). The recombinant strain with S. fibuligera ${\beta}$-glucosidase could metabolize cellobiose with a specific growth rate similar to the control strain in glucose. This recombinant strain showed higher hydrolysis efficiency in the cellulose simultaneous saccharification and fermentation, when using the Trichoderma reesei cellulase, which is short of the ${\beta}$-glucosidase activity. The final ethanol concentration was 110% (using Avicel) and 89% (using acid-pretreated corncob) higher than the control strain. These results demonstrated the effect of ${\beta}$-glucosidase secretion in the recombinant S. cerevisiae for enhancing cellulosic ethanol conversion.

Whole Cell Bioconversion of Ricinoleic Acid to 12-Ketooleic Acid by Recombinant Corynebacterium glutamicum-Based Biocatalyst

  • Lee, Byeonghun;Lee, Saebom;Kim, Hyeonsoo;Jeong, Kijun;Park, Jinbyung;Park, Kyungmoon;Lee, Jinwon
    • Journal of Microbiology and Biotechnology
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    • v.25 no.4
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    • pp.452-458
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    • 2015
  • The biocatalytic efficiency of recombinant Corynebacterium glutamicum ATCC 13032 expressing the secondary alcohol dehydrogenase of Micrococcus luteus NCTC2665 was studied. Recombinant C. glutamicum converts ricinoleic acid to a product, identified by gas chromatography/mass spectrometry as 12-ketooleic acid (12-oxo-cis-9-octadecenoic acid). The effects of pH, reaction temperature, and non-ionic detergent on recombinant C. glutamiucm whole cell bioconversion were examined. The determined optimal conditions for production of 12-ketooleic acid are pH 8.0, 35℃, and 0.05 g/l Tween80. Under these conditions, recombinant C. glutamicum produces 3.3 mM 12-ketooleic acid, with a 72% (mol/mol) maximum conversion yield, and 1.1 g/l/h volumetric productivity in 2 h; and 3.9 mM 12-ketooleic acid, with a 74% (mol/mol) maximum conversion yield, and 0.69 g/l/h maximum volumetric productivity in 4 h of fermentation. This study constitutes the first report of significant production of 12-ketooleic acid using a recombinant Corynebacterium glutamicum-based biocatalyst.

Enhanced Production of Succinic Acid by Actinobacillus succinogenes using the Production Medium Supplemented with Recombinant Carbonic Anhydrases (재조합 탄산무수화 효소 첨가 생산배지를 이용한 Actinobacillus succinogenes 유래의 숙신산 생산성 향상)

  • Park, Sang-Min;Eum, Kyuri;Kim, Sangyong;Jeong, Yong-Seob;Lee, Dohoon;Chun, Gie-Taek
    • KSBB Journal
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    • v.29 no.3
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    • pp.155-164
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    • 2014
  • Succinic acid, a representative biomass-derived platform chemical, is a major fermentation product of Actinobacillus succinogenes. It is well known that carbon dioxide is consumed during the succinate fermentation, but the biochemical mechanism behind this phenomenon is not yet understood well. In this study, it was found that the addition of carbonic anhydrase (CA)s into media significantly enhances the succinic acid production by A. succinogenes during the fermentation supplied with carbon dioxide. It is likely that the (bi) carbonate produced by the CA activity from gaseous carbon dioxide is favoured by A. succinogenes for consumption and utilization. Therefore, the $MgCO_3$ requirement could be significantly reduced without compromising the succinate productivity. Furthermore, because of too high price of the commercial carbonic anhydrase, it was undertaken to economically overproduce a cyanobacterial carbonic anhydrase by the use of a recombinant Pichia pastoris. An expression vector system was constructed with the carbonic anhydrase gene PCR-cloned from Cyanobacterium Synechocystis sp., and introduced into P. pastoris for fermentation studies. About 95.9 g/L of succinic acid was produced in the production medium with 30 ppm of carbonic anhydrase, approximately 2 fold higher productivity compared to the parallel process with no supplementation of the enzyme. It is expected that this method can provide a valuable way of overcoming inefficiencies inherent in gas supply during $CO_2$-based bioprocesses like succinic acid fermentation.

On-line Induction of Fermentation with Recombinant Cells: Part II. Control Algorithm and Software Development (유전자 재조합 세포 발효의 온.라인 유도 : 제 2부. 제어 알고리즘 및 소프트웨어 개발)

  • 이철균;최차용
    • KSBB Journal
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    • v.4 no.3
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    • pp.203-207
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    • 1989
  • Software for the on-line feedback control of such variables as DO and temperature was developed and tested successfully for a real fermentation system. Several aspects like Pl, PID, DSC, and DDC were incorporated into the algorithm. Any kind of on-line computer control system can be successfully implemented without much difficulty.

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Construction of Expression Vector of Bacillus sp. SSA3 Strain (Bacillus sp. SSA3 균주의 Expression Vector 개발)

  • 조윤래;김종규;권대준
    • Microbiology and Biotechnology Letters
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    • v.20 no.6
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    • pp.637-641
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    • 1992
  • The promoter regions from chromosomal DNA of Bacillus sp. SSA3 which is responsible for fermentation of Korean traditional soy sauce, were cloned for construction of expression vector of Bacills sp. SSA3. Recombinant plasmids were constructed by insertion of HindIIl-cleaved Bacillus sp. SSA3 chromosomal DNA fragments in front of the CAT gene of pGR71 plasmid and B-galactosidase gene of pUC18 plasmid. 6 recombinant plasmids were isolated from chloramphenicol resistant E. coli JM109 clones. All these plasmids were found to have promoter activity in Bacills sp. SSA3 and E. coli JM109. When these 6 clones of Bacills sp. SSA3 were cultivated in LB agar medium supplemented with 10% NaCI. fused CAT gene expression of 4 clones was significantly decreased in common. But the others were poorly inhibited.

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