• 제목/요약/키워드: high cell density culture

검색결과 175건 처리시간 0.033초

Production of Recombinant Polyhedra Containing Cry1Ac Fusion Protein in Insect Cell Lines

  • Kim, Jae-Su;Choi, Jae-Young;Roh, Jong-Yul;Lee, Han-Young;Jang, Seung-Sik;Je, Yeon-Ho
    • Journal of Microbiology and Biotechnology
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    • 제17권5호
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    • pp.739-744
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    • 2007
  • Insect cell lines and the control of infection for obtaining the maximum amount of polyhedrin-Cry1Ac-polyhedrin fusion protein from Bactrus in monolayer and suspension culture systems were tested. Growth rates of the Trichoplusia ni(High-Five) cell line in both culture systems were better than the other insect cell lines, Spodoptera frugiferda(Sf-9, Sf-21), Trichoplusia ni(Tn5), and Spodoptera exigua(Se301). The expression of the fusion protein in a monolayer culture showed that Se301 cells were 2.3-4.8 times more productive on a per cell basis than the other cell lines. However, in suspension culture, only High-Five cells were productive. High-Five cells infected with Bactrus at a multiplicity of infection(MOI) of 5 and a cell density of $3.0{\times}10^5$ cells per ml were more productive than the other infection condition in a suspension culture suitable for a large-scale production of baculovirus. In conclusion, for the large-scale production of Bactrus in vitro, High-Five cells showing good growth and high productivity are suitable.

고농도 재조합 대장균의 Fed-batch 배양 시스템을 이용한 Pyruvate Dehydrogenase Complex-E2 특이성 인간 모노클론 항체의 생산 (Production of Pyruvate Dehydrogenase Complex-E2 Specific Human Monoclonal Antibody in Fed-batch Culture Systems with High Cell Density Recombinant Escherichia coli)

  • 이미숙;전주미;차상훈;정연호
    • KSBB Journal
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    • 제15권5호
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    • pp.489-496
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    • 2000
  • 고농도 유전자 재조합 대장균을 이용하여 pyruvate dehy-drogenase complex-E2 특이성 인간 모노클론 항체의 Fab 부분을 효율적으로 생산하기 위해 회분식, 이단 연속식, 반 유 가식, two-stage cyclic fed-batch 동 여러 가지 배양 방법이 조사되었다. 먼저 플라스미드 안정성 문제를 극복하기 위해 growth stage와 production stage를 분리하는 two-phase 회분식 배양과 이단 연속식 시스템을 시도하였다 그 결과 two-phase 회분식 배양보다는 이단 연속식 배양에서의 세포농도와 항체 생산성이 우수하였다 또한 이단 연속식 배양에서의 세포 성 장과 항처l 생산성은 용존산소를 제어한 경우가 그렇지 않은 경우보다 월등하게 높았다. 그리고 plasmid 안정성에 있어서 는 실험기간 내에 거의 100%를 유지하여 높은 안정도를 보 여주었다. 유가식 공정에 적합한 공급 배지로 변형된 M9 배 지가 최적배지로 선정되었고 이 배지 중 최적의 CjN 비율을 조사한 결파 2:3으로 결정되었다. 반 유가식 시스템에서 constant feeding 전략을 사용할 경우 최적 공급속도는 $0.6g/\ell/hr$이었다. 또한 pulse에 의해 공급배지를 공급할 경우에는 총 공급 량이 같을 경우 소량으로 자주 공급해 주는 것이 공급배지를 한꺼번에 많은 양을 공급해주는 것 보다 바람직하였다. 여러 가지 feeding 전략을 조사해 본 결과 linear feeding 방법이 가장 효과적이었다. 하지만 linear feeding 방법마저도 고농도 세포배양에 한계가 있었기 때문에 pH-stat 방법을 이용한 two-stage cyclic fed-batch 시스템을 시도하여 $54 g/\ell$의 세포 를 얻을 수 있었다. 따라서 이 방법이 일단 생산성 향상을 위한 세포의 고농도 배양에는 조사한 여러 배양 시스템 중에 가장 효율적인 시스템임올 알 수 있었다 하지만 이 시스템 에서 포도당을 낮은 level로 유지할 수 있었으나, 초산의 과도한 축적으로 항체 생산성의 향상은 예상에 비해 크지 않았다.

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Linear Correlation between Online Capacitance and Offline Biomass Measurement up to High Cell Densities in Escherichia coli Fermentations in a Pilot-Scale Pressurized Bioreactor

  • Knabben, Ingo;Regestein, Lars;Schauf, Julia;Steinbusch, Sven;Buchs, Jochen
    • Journal of Microbiology and Biotechnology
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    • 제21권2호
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    • pp.204-211
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    • 2011
  • To yield high concentrations of protein expressed by genetically modified Escherichia coli, it is important that the bacterial strains are cultivated to high cell density in industrial bioprocesses. Since the expressed target protein is mostly accumulated inside the E. coli cells, the cellular product formation can be directly correlated to the bacterial biomass concentration. The typical way to determine this concentration is to sample offline. Such manual sampling, however, wastes time and is not efficient for acquiring direct feedback to control a fedbatch fermentation. An E. coli K12-derived strain was cultivated to high cell density in a pressurized stirred bioreactor on a pilot scale, by detecting biomass concentration online using a capacitance probe. This E. coli strain was grown in pure minimal medium using two carbon sources (glucose and glycerol). By applying exponential feeding profiles corresponding to a constant specific growth rate, the E. coli culture grew under carbon-limited conditions to minimize overflow metabolites. A high linearity was found between capacitance and biomass concentration, whereby up to 85 g/L dry cell weight was measured. To validate the viability of the culture, the oxygen transfer rate (OTR) was determined online, yielding maximum values of 0.69 mol/l/h and 0.98mol/l/h by using glucose and glycerol as carbon sources, respectively. Consequently, online monitoring of biomass using a capacitance probe provides direct and fast information about the viable E. coli biomass generated under aerobic fermentation conditions at elevated headspace pressures.

배양 조건에 따른 식물세포 크기 지수의 변화 (Changes of Plant Cell Size Index by Culture Conditions)

  • 김상목;박인석;이상윤;이규화;김동일
    • KSBB Journal
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    • 제13권4호
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    • pp.438-443
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    • 1998
  • Effects of various environmental factors on cell size index(FCW/DCW) in Thalictrum rugosum. Lithospermum erythrorhizon and Taxus cuspidata plant cell suspension cultures were investigated. Time course change of cell size index were also observed. In batch cultures, FCW/DCW increased according to the decrease of sugar concentration. For short-term experiment within 24 hr, FCW/DCW value could be reduced significantly by increasing sugar concentration. When an osmoticum such as mannitol was added, FCW/DCW converged to a low value. Therefore, it was confirmed that osmolality of the medium was important in determining cell size or water content of the cells. Inorganic salts or treatment with organic solvent also exhibited some effect on the cell size index. However, pH and centrifugal force did not show any influences. On the other hand, it was found that the addition of Pluronic F-68 reduced FCW/DCW. By combining these results effectively, it may be possible to increase the cell concentration in high density culture to a higher extent.

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Microencapsulation에 의한 미세조류의 고밀도 배양 (High-Density Cultivation of Microalgae using Microencapsulation)

  • 한영호;이정석;곽중기;이응호;조만기
    • 한국수산과학회지
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    • 제32권2호
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    • pp.186-191
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    • 1999
  • 본 연구에서는 미세조류의 고밀도 배양을 위한 경제적인 공정을 개발하는 차원에서 3종의 미세조류 즉, Chlorella vulgaris, Dunaliella salina 및 Porphyridium purpureum를 Ca-alginate 로 microencapsulation 한 후 air-bubble column형 배양조에서 고밀도 배양을 시도하였다. $2\%\;CaCl_2$ 농도로 capsule을 제조할 때 capsule의 안정성이 가장 좋았으며, capsule 막의 두께 및 $CO_2$ 공급유무에 따른 미세조류 (Chlorella vulgaris)의 생산성은 거의 차이가 없었다. 한편, 3종의 미세조류 모두 capsule로 고정화시킨 것이 bead로 고정화한 미세조류나 free cell 보다 농도가 높았으며, 특히Dunaliella salina가 microencapsulation에 의한 고밀도 배양 효과가 가장 뛰어나 free cell 보다 약 5배 정도의 생산성을 나타내었다.

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Enhanced Production of Human Serum Albumin by Fed-Batch Culture of Hansenula polymorpha with High-Purity Oxygen

  • Youn, Jong-Kyu;Shang, Longan;Kim, Moon-Il;Jeong, Chang-Moon;Chang, Ho-Nam;Hahm, Moon-Sun;Rhee, Sang-Ki;Kang, Hyun-Ah
    • Journal of Microbiology and Biotechnology
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    • 제20권11호
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    • pp.1534-1538
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    • 2010
  • Fed-batch cultures of Hansenula polymorpha were studied to develop an efficient biosystem to produce recombinant human serum albumin (HSA). To comply with this purpose, we used a high-purity oxygen-supplying strategy to increase the viable cell density in a bioreactor and enhance the production of target protein. A mutant strain, H. polymorpha GOT7, was utilized in this study as a host strain in both 5-l and 30-l scale fermentors. To supply high-purity oxygen into a bioreactor, nearly 100% high-purity oxygen from a commercial bomb or higher than 93% oxygen available in situ from a pressure swing adsorption (PSA) oxygen generator was employed. Under the optimal fermentation of H. polymorpha with highpurity oxygen, the final cell densities and produced HSA concentrations were 24.6 g/l and 5.1 g/l in the 5-l fermentor, and 24.8 g/l and 4.5 g/l in the 30-l fermentor, respectively. These were about 2-10 times higher than those obtained in air-based fed-batch fermentations. The discrepancies between the 5-l and 30-l fermentors with air supply were presumably due to the higher contribution of surface aeration over submerged aeration in the 5-l fermentor. This study, therefore, proved the positive effect of high-purity oxygen in enhancing viable cell density as well as target recombinant protein production in microbial fermentations.

고농도 세포배양에서 Bacillus thuringiensis의 세포 성장과 포자 형성 속도 (Growth Kinetics and Sporulation of Bacillus thuringiensis in High Cell Density Culture)

  • 강병철;장호남
    • KSBB Journal
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    • 제16권1호
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    • pp.30-35
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    • 2001
  • 유가식배양과 세라믹 막을 장착한 생물반응기에서 운전인 TCRC 조업을 통해서 Bacillus thuringiensis의 고농도 세포배양을 실시하였다. 유가식 배양에서 B. thuringiensis의 세포 성장은 선형적으로 증가하였고, 이것은 세포성장 모델리의 결과와 잘 맞았다. 낮은 세포 성장속에도 불구하고 유가식 배양동안에 포자형성은 관찰할 수 없었고, 이것은 연속배양의 결과와는 반대였다. 유가식 조업 후에 회분식 배양으로 바꾸면 300 g/L의 포도당 공급 농도를 사용했을 때 2.7$\times$$10^9$ CFU/mL 의 포자농도를 얻었다. 생물반응기내에 세라믹 막을 장착한 TCRC 조업에서 포도당 공급 농도의 영향을 결정하였다. 50 g/L의 포도당 농도를 사용했을 때 TCRC 조업에서 82.5 g-cell/L에 해당하는 최대 세포농도 1.8$\times$$10^{10}$ CFU/mL 를 얻었다. TCRC에서 세포성장은 선형적으로 증가하였고 포도당 농도는 제한되었는데 이것은 세포성장은 모델링의 결과와 잘 일치하였다. 1 g/L의 포도당을 공급한 경우 이외에는 TCRC 조업 동안에 포자형성을 관찰할 수 없었다. 50 g/L의 포도당을 공급한 경우 TCRC조업 후에 회분식 배양으로 전환시키면 1.2$\times$$10^{10}$ CFU/mL 의 포자농도를 얻었고, 이것은 연구된 여러 배양형태 중에 가장 높은 포자농도이다. 이 때 최적의 포도당 공급속도는 0.55 g glucose/h로 공급하였을 때였다.

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A New Spin Filter for High Density Culture and Ethanol Production by Saccharomyces cerevisiae

  • Moon, Hyun-Soo;Lim, Dong-Joon;Song, Gu-Young;Kang, Hyun-Ah;Kim, Seung-Wook;Kim, Ik-Hwan;Hong, Suk-In
    • Journal of Microbiology and Biotechnology
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    • 제12권3호
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    • pp.406-410
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    • 2002
  • A new spin filter consisting of $50{\mu}m$ (nominal pore size) depth fitters rolled on a stainless steel grid was developed, using Saccharomyces cerevisiae as a model suspension cell to evaluate the spin filter performance. In a 1.8-1 fermentor with a rotation speed of 300 rpm and perfusion rate of 4 ml/min, a cell concentration of 49 g/l and ethanol concentration of 45 g/l from 100 g/l glucose could be obtained in a perfusion culture. The major mechanisms for cell separation used by the large-pore spin filter appeared to be centrifugal force and pivotal movement of the cells in the spin filter.

Fed-batch Fermentation for Production of Nitrile Hydratase by Rhodococcus rhodochrous M33

  • Kim, Bu-Youn;Kim, Jong-Chul;Lee, Hyune-Hwan;Hyun, Hyung-Hwan
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제6권1호
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    • pp.11-17
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    • 2001
  • To enhance the productivity and activity of nitrile hydratase in Rhodococcus rhodochrous M33, a glucose-limited fed-batch culture was performed. In a fed-batch culture where the glucose was controlled at a limited level and cobalt was supplemented during the fermentation period, the cell mass and total activity of nitrile hydratase both increased 3.3-fold compared to that in the batch fermentation. The productivity of nitrile hydratase also increased 1.9-fold compared to that in the batch fermentation. The specific activity of nitrile hydratase in the whole cell preparation when using a fed-batch culture was 120 units/mg-DCW, which was similar to that in the batch culture.

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Enhanced production in recycle fed-batch cultivation by Lactic acid bacteria Isolated from Kimchi

  • Joe, Lim;Kwun, Kyu-Hyuk;Chang, Hae-Choon;Lee, Jung-Heon
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2005년도 생물공학의 동향(XVII)
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    • pp.312-315
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    • 2005
  • A process for efficient recycle fed-batch culture was carried out to increase cell mass and spore production by Lactic acid bacteria isolated from Kimchi. A large quantity of cell mass obtained by feeding concentration of sugar in recycle fed-batch culture. When the high density of salt was created that the cell mass was come-down. In this study, cultured in different feeding concentration of sugar conditions. Lactic acid bacteria by recycle fed-batch culture was investigated in 2L working volume of fermenter, obtained the maximum cell mass was 15.17g/L.

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