谷氨酰胺对微囊化重组CHO细胞生长代谢及内皮抑素表达的影响

微囊化技术是一种有发展潜力的生物技术,在细胞移植和药物控释等方面具有广泛的应用。然而由于目前微囊化细胞规模化培养技术还不成熟,阻碍了其在临床治疗中的推广与应用。为了了解微囊化重组CHO细胞的生长代谢特性为今后规模化培养优化提供技术参考,考察了主要氮源物质谷氨酰胺对微囊化重组CHO细胞生长代谢及内皮抑素表达的影响。结果显示:当谷氨酰胺起始浓度从2.69mmolL增加到9.05mmolL时最大活细胞密度并没有增高,细胞增殖没有显著差异。当谷氨酰胺起始浓度较低(2.69mmolL)时,葡萄糖的比消耗速率较大;当谷氨酰胺起始浓度增高时(7.91mmolL～9.05mmolL)葡萄糖和谷氨酰胺的比消耗速率增大,但细胞对葡萄糖和谷氨酰胺的利用率降低。谷氨酰胺对产物表达有显著影响,起始浓度为4.97mmolL时的内皮抑素累积浓度最高,达546.36ngmL,过低和过高谷氨酰胺起始浓度下内皮抑素的累积浓度均较低。     

重组CHO细胞培养过程中氨对细胞代谢的影响

研究了重组CHO细胞批培养过程中,氨浓度对细胞的葡萄糖、谷氨酰胺及其它氨基酸代谢的影响。表明,细胞对葡萄糖和谷氨酰胺的得率系数随着氨浓度的增加而降低,起始氨浓度为566mmol/L的批培养过程与起始氨浓度为021mmol/L的批培养过程相比,细胞对葡萄糖和谷氨酰胺的得率系数分别下降了78%和74%,细胞对其它氨基酸的得率系数也分别下降了50%～70%。氨浓度的增加明显地改变了细胞的代谢途径,葡萄糖代谢更倾向于厌氧的乳酸生成。在谷氨酰胺的代谢过程中,谷氨酸经谷氨酸脱氢酶进一步生成α酮戊二酸的过程受到了氨的抑制,而氨对谷氨酸经谷氨酸转氨酶反应生成α酮戊二酸的过程有促进作用,但总体上谷氨酸进一步脱氨生成α酮戊二酸的反应受到了氨的限制。     

Catabolic control of hybridoma cells by glucose and glutamine limited fed batch cultures

Substrate limited fed batch cultures were used to study growth and overflow metabolism in hybridoma cells. A glucose limited fed batch, a glutamine limited fed batch, and a combined glucose and glutamine limited red batch culture were compared with batch cultures. In all cultures mu reaches its maximum early during growth and decreases thereafter so that no exponential growth and decreases thereafter so that no exponential growth rate limiting, although the glutamine concentration (>0.085mM) was lower than reported K(s) vales and glucose was below 0.9mM; but some other nutrients (s) was the cause as verified by simulations. Slightly more cells and antibodies were produced in the combined fed batch compared with the batch culture. The specific rates for consumption of glucose and glutamine were dramatically influenced in fed batch cultures resulting in major metabolic changes. Glucose limitation decreased lactate formation, but increased glutamine consumption and ammonium formation. Glutamine limitation decreased ammonium and alanine formation of lactate, alanine, and ammonium was negligible in the dual-substrate limited fed batch culture. The efficiency of the energy metabolism increased, as judged by the increase in the cellular yield coefficient for glucose by 100% and for glutamine by 150% and by the change in the metabolic ratios lac/glc, ala/ln, and NH(x)/ln, in the combined fed culture. The data indicate that a larger proportion of consumed glutamine enters the TCA cycle through the glutamate dehydrogenase pathway, which releases more energy from glutamine than the transamination pathway. We suggest that the main reasons for these changes are decreased uptake rates of glucose and glutamine, which in turn lead to a reduction of the pyruvate pool and a restriction of the flux through glutaminase and lactate dehydrogenase. There appears to be potential for further cell growth in the dual-substrate-limited fed batch culture as judged by a comparison of mu in the different cultures. (c) 1994 John Wiley & Sons, Inc.     

Suspension culture process of MethA tumor cell for the production of heat-shock protein glycoprotein 96: process optimization in spinner flasks

Heat-shock proteins (HSPs) act like "chaperones", making sure that the cell's proteins are in the right shape and in the right place at the right time. Heat-shock protein glycoprotein 96 (gp96) is a member of the HSP90 protein family, which chaperones a number of molecules in protein folding and transportation. Heat-shock protein gp96 serves as a natural adjuvant for chaperoning antigenic peptides into the immune surveillance pathways. Currently, heat-shock protein gp96 was only isolated from murine and human tissues and cell lines. An animal cell suspension culture process for the production of heat-shock protein gp96 by MethA tumor cell was developed for the first time in spinner flasks. Effects of culture medium and condition were studied to enhance the MethA tumor cell density and the production and productivity of heat-shock protein gp96. Initial glucose concentration had a significant effect on the heat-shock protein gp96 accumulation, and an initial glucose level of 7.0 g/L was desirable for MethA tumor cell growth and heat-shock protein gp96 production and productivity. Cultures at an initial glutamine concentration of 3 and 6 mM were nutritionally limited by glutamine. At an initial glutamine concentration of 6 mM, the maximal viable cell density of 19.90 x 10(5) cells/mL and the maximal heat-shock protein gp96 production of 4.95 mg/L was obtained. The initial concentration of RPMI 1640 and serum greatly affected the MethA tumor cell culture process. Specifically cultures with lower initial concentration of RPMI 1640 resulted in lower viable cell density and lower heat-shock protein gp96 production. At an initial serum concentration of 8%, the maximal viable cell density of 19.18 x 10(5) cells/mL and the maximal heat-shock protein gp96 production of 5.67 mg/L was obtained. The spin rate significantly affected the cell culture process in spinner flasks, and a spin rate of 150 rpm was desirable for MethA tumor cell growth and heat-shock protein gp96 production and productivity. Not only the cell density but also the production and productivity of heat-shock protein gp96 attained in this work are the highest reported in the culture of MethA tumor cell. This work offers an effective approach for producing heat-shock protein glycoprotein 96 from the cell culture process. The fundamental information obtained in this study may be useful for the efficient production of heat-shock protein by animal cell suspension culture on a large scale.     

Metabolic and immune responses in Chinese mitten-handed crab (Eriocheir sinensis) juveniles exposed to elevated ambient ammonia

The toxicity of ammonia to Eriocheir sinensis juveniles was determined. The 24 h-, 48 h-, 72 h-, 96 h-LC(50) values of total ammonia (TAN) were 251.68, 217.61, 156.05, and 119.67 mg L(-1), respectively. Following these results, crabs were then exposed for a 2-day period to 20, 40, 60 and 80 mg L(-1) TAN and sampled at 3, 6, 24 and 48 h for changes in metabolic parameters (including haemolymph ammonia concentration, glucose, lactate, urea, triacylglycerol, glutamine, and glutamate levels) and immunity indicators (the total of haemocyte count and superoxide dismutase activity). Results showed a distinct linear relationship between ambient ammonia and haemolymph ammonia and a notable increase in haemolymph ammonia content after ammonia exposure. Compared with the control group, lower concentration of triglycerides and significantly higher glucose, urea, and lactate level in haemolymph were observed when ambient ammonia increased. This suggested a reduced use of carbohydrates through anaerobic metabolism and an increase in the use of lipids to satisfy the metabolic demand. A significant surge of the ammonia metabolic product, glutamate, was observed after 3 h ammonia exposure, and the compensatory response to reduced glutamate was manifested by increased glutamine synthesis. During the same period, total haemocyte count decreased while ambient ammonia increased. Superoxide dismutase (SOD) activity in haemolymph was stimulated by lower ambient ammonia concentration after short time exposure and depressed by higher ammonia concentration. Therefore, haemolymph ammonia accumulation resulted in an increase in energy demand and a depression in immune capacity. The mechanism to detoxification of ammonia may be to transform ammonia to urea and glutamine.     

固定化氧化亚铁硫杆菌培养条件对黄铁矾沉淀的影响

以聚乙烯醇-海藻酸钠复合材料为载体,Ca(NO3)2为交联剂对氧化亚铁硫杆菌进行包埋固定化。该固定化细胞的连续培养技术可以用于处理H2S、SO2,为了减少减少固定化细胞培养过程中带来许多不利效应的黄铁矾沉淀 (NH4Fe3(SO4)2(OH)6）,采取了改变初始pH值和目前普遍采用的9K培养基中的(NH4)2SO4浓度,K2HPO4浓度三种方法。结果显示：在三种方法中,降低(NH4)2SO4浓度是比较可行的一种方法,当(NH4)2SO4从3.0 g/L降低到0.5g/L,Fe2+氧化速率几乎没有受到影响,沉淀形成速率却减少了45%。在固定化细胞连续运行时,降低9K培养基中(NH4)2SO4的含量,当稀释率为0.4 h-1,运行时间为96 h,Fe2+氧化速率高达3.75 g/L.H,结果显示反应柱内沉淀明显减少,同时Fe2+氧化速率并没有明显变化。     

Physiological basis of the selective advantage of a Spirillum sp. in a carbon-limited environment

A Spirillum sp. and a Pseudomonas sp. possessing crossing substrate saturation curves for L-lactate were isolated from fresh water by chemostat enrichment. Their Ks and mumax values for L-lactate were: Spirillum sp., 23 micrometer and 0.35 h-1, respectively; Pseudomonas sp., 91 micrometer and 0.64 h-1, respectively. Under L-lactate limitation, pseudomonas sp. outgrew Spirillum s. at dilution rates (D) above 0.29 h-1, but the converse occurred at lower D values. The advantage of Spirillum sp. increased with decreasing D until, at D = 0.05 h-1 (i.e. L-lactate concentration of approximately 1 micrometer), Pseudomonas sp. was eliminated from the culture essentially as a non-growing population. In Spirillum sp. the Km for L-lactate transport (5.8 micrometer) was threefold lower than in Pseudomonas sp. (20 micrometer); Spirillum sp. also possessed a higher Vmax for the transport of this substrate. The surface to volume ratio was higher in Spirillum sp. and increased more markedly than in Pseudomonas sp. in response to decreasing D. Thus, a more efficient scavenging capacity contributes to the advantage of Spirillum sp. at low concentrations of the carbon source. Although most of the enzymes of L-lactate catabolism were more active in Pseudomonas sp., NADH oxidase activity was about twice as high in Spirillum sp.; and, unlike Pseudomonas sp., the cytochrome c content of this bacterium increased markedly with decreasing D. A more active and/or more efficient respiratory chain may therefore also play a role in the advantage of Spirillum sp. The other factors which appear to be involved include a lower energy of maintenance of Spirillum sp. [0.016 g L-lactate (g cell dry wt)-1 h-1 compared with 0.066 in Pseudomonas sp.] and a lower minimal growth rate.     

Optimization of virus yield as a strategy to improve rabies vaccine production by Vero cells in a bioreactor

To improve rabies vaccine production by Vero cells, we have developed a strategy based on high cell density culture and optimization of virus yield. We have first optimized cell growth in spinner flask using a Taguchi's L8 experimental design. We analyzed the effects of the following factors: initial glucose and glutamine concentrations, Cytodex 1 concentration and the regulation of glucose level at 1 g l(-1). We have also investigated the effect of the following factor interactions: Cytodex 1 concentration/glutamine concentration, Cytodex 1 concentration/glucose concentration and glucose concentration/glutamine concentration. Statistical analysis of the collected data pointed to the initial glucose concentration, the regulation of glucose level at 1 g l(-1) and the interactions between Cytodex 1 concentration/initial glucose concentration and Cytodex 1 concentration/initial glutamine concentration as the parameters that affected cell growth. Using the optimal conditions determined earlier, we have studied Vero cell growth in a 7-l bioreactor and in batch culture, and obtained a cell density level equal to 3.6 +/- 0.2 x 10(6) cells ml-1. Cell infection with rabies virus (LP 2061/Vero strain) at a multiplicity of infection (MOI) of 0.3 using M199 medium supplemented with 0.2% bovine serum albumin (BSA), yielded a maximal virus titer equal to 8 +/- 1.6 x 10(7) Fluorescent Focus Units (FFU) ml-1. We have also studied Vero cell growth in a 7-l bioreactor using recirculation as a perfusion culture mode during cell proliferation step and perfusion for virus multiplication phase. In comparison to batch culture, we reached a higher cell density level that was equal to 10.1 +/- 0.5 x 10(6) cells ml-1. Cell infection under the conditions previously indicated, yielded 14l of virus harvest that had a virus titer equal to 2.6 +/- 0.5 x 10(7) FFU ml-1. The activity of the inactivated virus harvest showed a protective activity that meets WHO requirements.     

Vancomycin production is enhanced in chemostat culture with biomass-recycle

Production of the glycopeptide antibiotic vancomycin by Amycolatopsis orientalis ATCC 19795 was examined in phosphate-limited chemostat cultures with biomass-recycle, employing an oscillating membrane separator, at a constant dilution rate (D= 0. 14 h-1). Experiments made under low agitation conditions (600 rpm) showed that the biomass concentration could be increased 3.9-fold with vancomycin production kinetics very similar to that of chemostat culture without biomass-recycle. The specific production rate (qvancomycin) was maximal when the biomass-recycle ratio (R) was 0.13 (D= 0.087 h-1). When the dissolved oxygen tension dropped below 20% (air saturation), the biomass and vancomycin concentrations decreased and an unidentified red metabolite was released into the culture medium. Using increased agitation (850 rpm), used to maintain the dissolved oxygen tension above 20% air saturation, maximum increases in biomass concentration (7.9-fold) and vancomcyin production 1.6-fold (0.6 mg/g dry weight/h) were obtained when R was 0.44 (D= 0.056 h -1) compared to chemostat culture without biomass-recycle. Moreover, at this latter recycle ratio the volumetric vancomycin production rate was 14.7 mg/L/h (a 7-fold increase compared to chemostat culture without biomass-recycle). These observations encourage further research on biomass-recycling as a means of optimising the production of antibiotics.     

Effects of dissolved oxygen concentration on hybridoma growth and metabolism in continuous culture

Oxygen transport is a major limitation in large-scale mammalian cell culture. The effects of the dissolved oxygen concentration (DO; from 0.1 to 100% saturation with air) on Sp2/0-derived mouse hybridomas were investigated using continuous culture. The steady-state concentration of viable cells increased with decreasing DO until a critical dissolved oxygen concentration of 0.5% of air saturation was reached. The cell concentration declined at lower DO because of incomplete glutamine oxidation, and the specific lactate production from glucose increased to offset the reduced energy production from glutamine. Cell viability increased as the DO was decreased; the viability continued to increase even when the DO was reduced below 0.5%. The specific oxygen uptake rate was essentially constant for DO greater than or equal to 10% of air saturation and then decreased with decreasing DO. The P/O ratio (ATP molecules produced per O atom consumed) appears to change from 2 to 3 between 10 and 0.5% DO. The specific ATP production rate calculated using this assumption decreases only slightly with decreasing DO. The optimum DO of 50% for antibody production is different than the optimum (approximately 0.5% DO) for cell growth.