• Title/Summary/Keyword: spin-filter bioreactor

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Insect Cell Culture for Recombinant $\beta$-galactosidase Production Using a Spin-filter Bioreactor

  • Chung, In-Sik;Kim, Hak-Ryul;Lee, Ki-Woong;Kim, Tae-Yong;Oh, Jai-Hyn;Yang, Jai-Myung
    • Journal of Microbiology and Biotechnology
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    • v.4 no.3
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    • pp.200-203
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    • 1994
  • Spodoptera frugiperda IPLB-SF-21-AE cells were cultivated in a spin-filter bioreactor with continuous perfusion for the recombinant $\beta$-galactosidase production. At the perfusion rate of 0.06 $hr^{-1}$, the maximum cell density of insect cells in this bioreactor system reached 3.5$\times$$l0^6$ viable cells/ml using the Grace media containing 5% FBS and 0.3% Pluronic F-68. The recombinant $\beta$-galactosidase production of 8, 100 units per reactor volume was also achieved at this perfusion rate.

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Continuous Propionic Acid Production from Cheese Whey Using In Situ Spin Filter

  • Gupta, Achin;Srivastava, Ashok K.
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.6 no.1
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    • pp.1-5
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    • 2001
  • The potential use of spin filter device to retain Propionibacterium acidipropionici in the bioreactor under continuous mode of fermentation, and improve acid productivity, was examined. The yield of propionic acid based on lactose concentration was 51% in batch and 54% in continuous (dilution rate = 0.05 h(sup)-1) operation. The yield in continuous fermentation with cell retention using spin filter of 10 micron size (dilution rate = 0.05 h(sup)-1) was even higher at 70% (w/w). The volumetric productivity under batch and continuous mode of operation were 0.312g L(sup)-1 h(sup)-1 and 0.718g L(sup)-1 h(sup)-1 respectively. Continuous fermentation with cell retention demonstrated even higher volumetric productivities at 0.98g L(sup)-1 h(sup)-1 with out clogging problems. It could be used for utilization of cheese whey to produce propionic acid at higher yield and productivities.

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Continuous Stable production of won Willerand Factor Monoclonal Antibody in Spin Filter Bioreactor with Bleeding Technology

  • Yun, Joung-Won;Lee, Soo-Young;Park, Byung-Wook;Han-Kyu oh;Kim, Se-Ho;Byum, Tea-Ho;Park, Soung-yong
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.5 no.2
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    • pp.130-135
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    • 2000
  • The characteristics of two different modes of perfusion culture, intermittent and continuous bleedings, were investigated by culturing the hybridoma cells producing von Willebrand Factor (vWF) monoclonal antibody (McAb) in a 15 L bioreactor without clogging the filter. Both culture methods exhibited similar profiles of cell density and metabolite concentrations during the culture period at the cell concentration of around 1${\times}$107 cells/mL. When the perfusion rate was increased, the intermittrnt bleeding culture showed problems of ammonia accumulation and decrease of cell viability. The continuous bleeding culture in terms of nutrient consumption and metabolite production kinetics. But the analysis of specific oxygen consumption rate showed that the specific oxygen consumption rate of intermittent bleeding culture was similar to that of exponential growth phase. The continuous bleeding culture showed higher specific oxygen consumption rate of intermittent bleeding culture. finally we proved the possibility of long-term operation of continuous bleeding culture and produced approximately 40 g of vWF McAb in a 15L bioreactor after one-month operation.

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Development of recombinant human chorionic gonadotropin (hCG) using high-density culture technique of suspension-adapted chinese hamster ovary (CHO) cells

  • Na, Kyu-Heum;Kim, Seung-Chul;Seo, Kwang-Seok;Lee, Sung-Hee;Kang, Soo-Hyung
    • 한국생물공학회:학술대회논문집
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    • 2005.04a
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    • pp.37-37
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    • 2005
  • Human chorionic gonadotropin (hCG) is a heterodimeric glycoprotein hormone consisting of non-covalently linked two subunits, the ${\alpha}$ and ${\beta}$ subunit. It has been used as a infertility drug for ovulation to mimic luteinizing hormone $(LH).^{1)}$ A stable cell line was established by transfection of Rc/CMV-i-dhfr-hCG, expression vector containing hCG ${\alpha}-$ and ${\beta}-genes$, into dihydrofolate reductase-deficient CHO cells and subesquent methotrexate-mediated gene amplification. Anchorage-dependent CHO cells were adapted into a serum-free and/or animal component-free suspension medium through gradual serum weaning for the hCG production. The established cell line showed typical morphological characteristics and growth profile of CHO cells, and could produce FSH with passage-to-passage consistency. The high density perfusion culture of the CHO cells was carried out in Celligen Plus bioreactor equipped with a spin-filter as a internal cell retention device. The cell density reached up to $>1x10^{7}$ cells/ml in less than 7 days and a perfusion-control strategy based on cellular consumption rates of glucose was $established.^{2)}$ Biologically active recombinant hCG was purified by a series of chromatographic steps including anion exchange chromatography and hydrophobic interaction chromatography to homogeneity. The highly purified recombinant hCG was characterized for physicochemical, immunological and biological properties.

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