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1.
Thomas I. Potgieter Sean D. Kersey Muralidhar R. Mallem Adam C. Nylen Marc d'Anjou 《Biotechnology and bioengineering》2010,106(6):918-927
Growth of the antibody market has fueled the development of alternative expression systems such as glycoengineered yeast. Although intact antibody expression levels in excess of 1 g L?1 have been demonstrated in glycoengineered yeast, this is still significantly below the titers reported for antibody fragments in fungal expression systems. This study presents a simplified approach to estimate antibody secretion kinetics and oxygen uptake rate requirements as a function of growth‐rate controlled by a limiting methanol feed rate in glycoengineered Pichia pastoris. The yield of biomass from methanol and the specific oxygen requirements predicted in this study compare well with values reported in the literature for wild‐type P. pastoris, indicating the intrinsic nature of these yields independent of glycoengineering or the heterologous protein expressed. Specific productivity was found to be a non‐linear function of specific growth rate. Based on comparison with relationships between specific growth rate and specific productivity reported in the literature this correlation seems empirical in nature and cannot be established a priori. These correlations were then used in a simple mass balance based model to predict the cultivation performance of carbon limited cultivations under oxygen transfer limited conditions to indicate the usefulness of this approach to predict large scale performance and aid in process development. Biotechnol. Bioeng. 2010;106: 918–927. © 2010 Wiley Periodicals, Inc. 相似文献
2.
Jahic M Knoblechner J Charoenrat T Enfors SO Veide A 《Biotechnology and bioengineering》2006,93(6):1040-1049
For improved interfacing of the Pichia pastoris fed-batch cultivation process with expanded bed adsorption (EBA) technique, a modified cultivation technique was developed. The modification included the reduction of the medium salt concentration, which was then kept constant by regulating the medium conductivity at low value (about 8 mS/cm) by salt feeding. Before loading, the low conductivity culture broth was diluted only to reduce viscosity, caused by high cell density. The concept was applied to a one-step recovery and purification procedure for a fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A fused to lipase B from Candida antarctica (CALB). The modified cultivation technique resulted in lower cell death and consequently lower concentration of proteases and other contaminating proteins in the culture broth. Flow cytometry analysis showed 1% dead (propidium-stained) cells compared to 3.5% in the reference process. During the whole process of cultivation and recovery, no proteolysis was detected and in the end of the cultivation, the product constituted 87% of the total supernatant protein. The lipase activity in the culture supernatant increased at an almost constant rate up to a value corresponding to 2.2 g/L of CBM-CALB. In the EBA process, no cell-adsorbent interaction was detected but the cell density had to be reduced by a two-times dilution to keep a proper bed expansion. At flow velocity of 400 cm/h, the breakthrough capacity was 12.4 g/L, the product yield 98%, the concentration factor 3.6 times, the purity about 90%, and the productivity 2.1 g/L x h. 相似文献
3.
The intracellular metabolic fluxes through the central carbon pathways in the bioprocess for recombinant human erythropoietin (rHuEPO) production by Pichia pastoris (Mut+) were calculated to investigate the metabolic effects of dual carbon sources (methanol/sorbitol) and the methanol feed rate, and to obtain a deeper understanding of the regulatory circuitry of P. pastoris, using the established stoichiometry‐based model containing 102 metabolites and 141 reaction fluxes. Four fed‐batch operations with (MS‐) and without (M‐) sorbitol were performed at three different constant specific growth rates (h?1), and denoted as M‐0.03, MS‐0.02, MS‐0.03, and MS‐0.04. Considering the methanol consumption pathway, the M‐0.03 and MS‐0.02 conditions produced similar effects and had >85% of formaldehyde flux towards the assimilatory pathway. In contrast, the use of the dual carbon source condition generated a shift in metabolism towards the dissimilatory pathway that corresponded to the shift in dilution rate from MS‐0.03 to MS‐0.04, indicating that the methanol feed exceeded the metabolic requirements at the higher µ0. Comparing M‐0.03 and MS‐0.03 conditions, which had the same methanol feeding rates, sorbitol addition increased the rHuEPO synthetic flux 4.4‐fold. The glycolysis, gluconeogenesis, and PPP pathways worked uninterruptedly only at MS‐0.02 condition. PPP and TCA cycles worked with the highest disturbances at MS‐0.04 condition, which shows the stress of increased feeding rates of methanol on cell metabolism. Biotechnol. Bioeng. 2010; 105: 317–329. © 2009 Wiley Periodicals, Inc. 相似文献
4.
An optimization method for repeated fed-batch fermentation was established with the aim of improving the recombinant human serum albumin (rHSA) production in Pichia pastoris. A simulation model for fed-batch fermentation was formulated and the optimal methanol-feeding policy calculated by dynamic programming method using five different methanol-feeding periods. The necessary state variables were collected from the calculated results and used for further optimization of repeated fed-batch fermentation. The optimal operation policy was investigated using the pre-collected state variables by estimating the overall profit per total methanol-feeding time. The calculated results indicated that the initial cell mass from the 2nd fed-batch fermentation on should be set at 35 or 40 g and methanol-feeding time at 264 h. In repeated fed-batch fermentation using the optimal operation policy, actual culture volume was in good agreement with the values simulated by model equations, but some discrepancy was observed in rHSA production. Minimum experiments were therefore carried out to re-evaluate rHSA production levels, which were then applied in re-calculations to determine the optimal operation policy. The optimal policy for repeated fed-batch fermentation established in the present study (i.e., 4-times-repeated fed-batch fermentation) achieved a 47% increase in annual rHSA production. Optimization of the culture period also brought about a 28% increase in annual rHSA production even in simple (not repeated) fed-batch fermentation. 相似文献
6.
Mohsin Ahmad Khan Nadeem Ahmed Muhammad Islam Khan Ahmad Usman Zafar Saad Tahir Muhammad Sohail Anjum 《Bioscience, biotechnology, and biochemistry》2017,81(6):1114-1119
Previously, we have reported cloning of human epidermal growth factor gene from Huh-7 cells and its extracellular expression in Pichia pastoris. The presented work is a detailed report regarding molecular characterization of Huh-7 cells-derived hEGF expressed in Pichia pastoris with special reference to its glycosylation profiling and bioactivity studies. Densitometric scanning of SDS-PAGE separated extracellular proteins from hEGF recombinant Pichia pastoris strain indicated that about 84% of the extracellular proteins were glycosylated. Size exclusion chromatography using Superdex 75 prep grade column was successfully utilized to separate fractions containing glycosylated and non-glycosylated extracellular proteins. In dot blot assay, hEGF was detected in both glycosylated and non-glycosylated fractions. Bioactivity assays revealed that both glycosylated and non-glycosylated fractions were bioactive as determined by cell viability assay. It was also observed that hEGF present in non-glycosylated fraction was relatively more bioactive than hEGF present in glycosylated fraction. 相似文献
7.
A predictive control algorithm coupled with a PI feedback controller has been satisfactorily implemented in the heterologous Rhizopus oryzae lipase production by Pichia pastoris methanol utilization slow (Mut(s)) phenotype. This control algorithm has allowed the study of the effect of methanol concentration, ranging from 0.5 to 1.75 g/L, on heterologous protein production. The maximal lipolytic activity (490 UA/mL), specific yield (11,236 UA/g(biomass)), productivity (4,901 UA/L . h), and specific productivity (112 UA/g(biomass)h were reached for a methanol concentration of 1 g/L. These parameters are almost double than those obtained with a manual control at a similar methanol set-point. The study of the specific growth, consumption, and production rates showed different patterns for these rates depending on the methanol concentration set-point. Results obtained have shown the need of implementing a robust control scheme when reproducible quality and productivity are sought. It has been demonstrated that the model-based control proposed here is a very efficient, robust, and easy-to-implement strategy from an industrial application point of view. 相似文献
8.
Simple cyclic fed-batch culture (cfbc), consisting of a constant medium feed with periodic withdrawals of culture, resulted in a product yield (13.4 mg protein per gram biomass) similar to that obtained using the complex multiphase industrial production strategy (13.7 mg protein per gram biomass). In cfbc, productivity was ultimately limited by the rate at which the cells could assimilate methanol. Glycerol was inhibitory to growth at high concentrations. However, product yield continued to increase as the glycerol concentration was increased. In chemostat culture, dissolved oxygen concentration influenced product yield independently of any detectable influence on cell growth. 相似文献
9.
本文对毕赤酵母进行了恒化培养研究。以甲醇为唯一碳源时,在稀释率较低时(D<0.048 h-1),连续培养系统操作很稳定。但在稀释率高时(D>0.048h-1),连续培养系统的定态点不止一个,实验不能维持,故采用比生长速率恒定的分批流加培养进行研究。结果表明,毕赤酵母的生长符合Andrew普遍化底物抑制模型。综合考虑水蛭素的生成、底物的消耗,在生产中维持甲醇浓度为限制性浓度(0.5 g/L),且维持比生长速率为0.02 h-1时,水蛭素Hir65的比生成速率达到最大值0.2 mg/(g·h)且甲醇的比消耗速率为0.04 g/(g·h)。 相似文献
10.
B‐cell maturation antigen (BCMA) fused at the C‐terminus to the Fc portion of human IgG1 (BCMA‐Fc) blocks B‐cell activating factor (BAFF) and proliferation‐inducing ligand (APRIL)‐mediated B‐cell activation, leading to immune disorders. The fusion protein has been cloned and produced by several engineering cell lines. To reduce cost and enhance production, we attempted to express recombinant human BCMA‐Fc (rhBCMA‐Fc) in Pichia pastoris under the control of the AOX1 methanol‐inducible promoter. To produce the target protein with uniform molecular weight and reduced immunogenicity, we mutated two predicted N‐linked glycosylation sites. The secretory yield was improved by codon optimization of the target gene sequence. After fed‐batch fermentation under optimized conditions, the highest yield (207 mg/L) of rhBCMA‐Fc was obtained with high productivity (3.45 mg/L/h). The purified functional rhBCMA‐Fc possessed high‐binding affinity to APRIL and dose‐dependent inhibition of APRIL‐induced proliferative activity in vitro through three‐step purification. Thus, this yeast‐derived expression method could be a low‐cost and effective alternative to the production of rhBCMA‐Fc in mammalian cell lines. 相似文献
11.
Muralidhar Mallem Shannon Warburton Fang Li Ishaan Shandil Adam Nylen Sehoon Kim Youwei Jiang Michael Meehl Marc d'Anjou Terrance A. Stadheim Byung‐Kwon Choi 《Biotechnology progress》2014,30(6):1488-1496
Human serum albumin (HSA) is a cysteine rich molecule that is most abundant in human blood plasma. To remain viable in the market due to lower marketing costs for HSA, it is important to produce a large quantity in an economical manner by recombinant technology. The objective of this study was to maximize recombinant HSA (rHSA) production using a Muts Pichia pastoris strain by fermentation process optimization. We evaluated the impact of process parameters on the production of rHSA, including induction cell density (wet cell weight, g/L) and the control of specific growth rate at induction. In this study, we demonstrated that induction cell density is a critical factor for high level production of rHSA under controlled specific growth rate. We observed higher specific productivities at higher induction cell densities (285 g/L) and at lower specific growth rates (0.0022–0.0024/h) during methanol induction phase, and achieved the broth titer of rHSA up to 10 g/L. The temperature shift from 24 to 28oC was effective to control the specific growth rate at low level (≤0.0024/h) during methanol induction phase while maintaining high specific productivity [0.0908 mgrHSA/(gwcw h)]. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1488–1496, 2014 相似文献
12.
《Bioscience, biotechnology, and biochemistry》2013,77(11):2334-2343
Various mutant lysozymes having the N-glycosylation signal sequence, R21T (Asn19-Tyr20-Thr21), G49N (Asn49- Ser50-Thr51), R21T/G49N (Asn19-Tyr20-Thr21/Asn49-Ser50-Thr51), were secreted in the Pichia pastoris expression system. The secreted amounts of these mutant glycosylated lysozymes were almost the same as those of wild-type lysozyme (about 30 mg/liter). Glycosylation of the mutant lysozymes was confirmed by SDS-PAGE patterns, Endo-H treatment, TOF-MS analysis and chemical analysis. The composition of the carbohydrate chain attached to the single glycosylated lysozymes, R21T and G49N, was GlcNAc2Man9-11, while that of the double glycosylated lysozyme, R21T/G49N, was GlcNAc4Man27-32. The results of a CD analysis and lytic activity suggested that the conformation of the single glycosylated lysozymes had been conserved, while that of the double glycosylated lysozyme was less stable. The emulsifying properties of the lysozyme when glycosylated were greatly improved, being especially noteworthy in the double glycosylated lysozyme. 相似文献
13.
猪生产激素基因在巴斯德毕赤酵母中的高效分泌表达及产物的N—糖基化分析 总被引:5,自引:0,他引:5
利用含有强启动子PAOX1和α-MF信号肽序列的巴斯德毕赤酵母载体质粒pPICZαA构建出含PST基因的重复组质粒pPICZαA-pST。通过电击将经SacI酶后线化的pPICZαA-pST质粒转化到巴斯德毕赤酵母X-33菌中,并筛选Mut^ 表型的重型的生组菌。表达产物的SDS-PAGE和Western blot结果表明,分泌于胞外的PST蛋白分子量比天然PST分子量稍大,而胞内的PST蛋白分子量与天然PST大小相同,将经SacI酶切后线性化的pPICZαA-pST再次转化重组酵母细胞X-33/pPICZαA-pST(Mut^ ),所得表达产物的SDS-PAGE和Western blot结果显示,PST基因的表达水平明显提高,且表达产生的蛋白均可发生正确的抗原-抗体结合反应,表达量达956mg/L。将发酵液上清进行N-糖基化分析,显示rPST无N-糖基化加工修饰。 相似文献
14.
Ye J Ly J Watts K Hsu A Walker A McLaughlin K Berdichevsky M Prinz B Sean Kersey D d'Anjou M Pollard D Potgieter T 《Biotechnology progress》2011,27(6):1744-1750
Glycoengineering enabled the production of proteins with human N-linked glycans by Pichia pastoris. This study used a glycoengineered P. pastoris strain which is capable of producing humanized glycoprotein with terminal galactose for monoclonal antibody production. A design of experiments approach was used to optimize the process parameters. Followed by further optimization of the specific methanol feed rate, induction duration, and the initial induction biomass, the resulting process yielded up to 1.6 g/L of monoclonal antibody. This process was also scaled-up to 1,200-L scale, and the process profiles, productivity, and product quality were comparable with 30-L scale. The successful scale-up demonstrated that this glycoengineered P. pastoris fermentation process is a robust and commercially viable process. 相似文献
15.
Effect of feed rate on growth rate and antibody production in the fed-batch culture of murine hybridoma cells 总被引:2,自引:0,他引:2
Batch and fed-batch cultures of a murine hybridomacell line (AFP-27) were performed in a stirred tankreactor to estimate the effect of feed rate on growthrate, macromolecular metabolism and antibodyproduction. Macromolecular composition was foundto change dynamically during batch culture ofhybridoma cells possibly due to active production ofDNA, RNA and protein during the exponential phase.Antibody synthesis is expected to compete with theproduction of cellular proteins from the amino acidpool. Therefore, it is necessary to examine therelationship between cell growth in terms of cellularmacromolecules and antibody production. In this study,we searched for an optimum feeding strategy bychanging the target specific growth rate in fed-batchculture to give higher antibody productivity whileexamining the macromolecular composition. Concentratedglucose (60 mM) and glutamine (20 mM) in DR medium(1:1 mixture of DMEM and RPMI) with additional aminoacids were fed continuously to the culture and thefeed rate was updated after every sampling to ensureexponential feeding (or approximately constantspecific growth rate). Specific antibody productionrate was found to be significantly increased in thefed-batch cultures at the near-zero specific growthrate in which the productions of cellular DNA, RNA,protein and polysaccharide were strictly limited byslow feeding of glucose, glutamine and other nutrients. Possible implications of these results are discussed. 相似文献
16.
Chee Furng Wong D Tin Kam Wong K Tang Goh L Kiat Heng C Gek Sim Yap M 《Biotechnology and bioengineering》2005,89(2):164-177
As we pursue the means to improve yields to meet growing therapy demands, it is important to examine the impact of process control on glycosylation patterns to ensure product efficacy and consistency. In this study, we describe a dynamic on-line fed-batch strategy based on low glutamine/glucose concentrations and its impact on cellular metabolism and, more importantly, the productivity and N-glycosylation quality of a model recombinant glycoprotein, interferon gamma (IFN-gamma). We found that low glutamine fed-batch strategy enabled up to 10-fold improvement in IFN-gamma yields, which can be attributed to reduced specific productivity of ammonia and lactate. Furthermore, the low glutamine concentration (0.3 mM) used in this fed-batch strategy could maintain both the N-glycosylation macro- and microheterogeneity of IFN-gamma. However, very low glutamine (<0.1 mM) or glucose (<0.70 mM) concentrations can lead to decreased sialylation and increased presence of minor glycan species consisting of hybrid and high-mannose types. This shows that glycan chain extension and sialylation can be affected by nutrient limitation. In addition to nutrient limitation, we also found that N-glycosylation quality can be detrimentally affected by low culture viability. IFN-gamma purified at low culture viability had both lower sialylation as well as glycans of lower molecular masses, which can be attributed to extensive degradation by intracellular glycosidases released by cytolysis. Therefore, in order to maintain good N-glycosylation quality, there is a need to consider both culture viability and nutrient control setpoint in a nutrient-limiting fed-batch culture strategy. A greater understanding of these major factors that affect N-glycosylation quality would surely facilitate future development of effective process controls. 相似文献
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溶栓剂DSPAα1正处于治疗急性缺血性中风的III期临床研究,临床结果显示DSPAα1具有良好的药理学和安全特性。将DSPAα1基因序列按照毕赤酵母偏好密码子进行优化,并在毕赤酵母菌株GS115和KM71中进行表达,同时利用定点突变对糖基化侧链进行缺失,考察糖基侧链对毕赤酵母表达DSPAα1的影响。结果表明,野生型DSPAα1在GS115和KM71中均获得高表达,在摇瓶发酵条件下,表达量分别为70mg/L和105mg/L;利用SDS-PAGE对DSPAα1三种突变体(N117Q、N362Q和N117Q/N362Q)进行分析,与野生型蛋白质相比较,3种突变体的表达水平显著下降,同时纤溶平板测活数据显示,纯化后的突变体N117Q和N362Q比活性均低于野生型蛋白质的25%。这表明,N-型糖链(N117和N362)对毕赤酵母表达的DSPAα1分泌和酶活性具有重要作用。 相似文献
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Hong Liang Zhao Qing He Chong Xue Bo Sun Xue Qin Yao & Zhi Min Liu 《FEMS yeast research》2009,9(4):591-599
Onconase, an RNAse extracted from embryos of the Northern leopard frog ( Rana pipiens ), is in a confirmatory phase IIIb clinical trial for the treatment of unresectable malignant mesothelioma. Because the current purification process for onconase is cumbersome and laborious, the development of more efficient and cost-effective alternative sources is imperative. In this study, we assessed the potential of Pichia pastoris as an expression host for the large-scale production of onconase. Because of its specific N-terminal structure, active onconase with a correct N-terminus could not be secreted by an α-mating factor (α-MF)-prepro secretion signal, and an α-MF-pre secretion signal should be used instead. Onconase accumulated to a high concentration (about 300 and 150 mg L−1 for glycosylated onconase and aglycosylated mutein, respectively) in high cell density fermentation, and was purified to homogeneity with high yields (56% for glycosylated onconase and 67% for aglycosylated mutein) by a simple purification process consisting of cation exchange chromatography and size exclusion chromatography. In vitro activity assays revealed that glycosylation decreased both the RNAse activity and the cytotoxic activity of onconase. The high expression level and subsequent facile purification process make P. pastoris an efficient and cost-effective host for the large-scale production of onconase. 相似文献