Analysis of Mass Isotopomer Distributions of Proteingenic Amino Acids Used GC-MS during ~(13)CMFA / 中国生物工程杂志

13C metabolic flux analysis(13CMFA)have been the research hotspots of metabolic engineering internationally due to its accuracy and applicability.It is vital that the measurement of 13C labelling pattern of proteinogenic amino acids for 13C metabolic flux analysis.To acquire 13C-labelling proteinogenic amino acids,Pseudomonas denitrifican which products Vitamin B12 was firstly fed with mimimal culture medium contained 20% U-13C and 80% natural glucose,after the culture reached a steady state,then about 20 mg biomass was hydrolyzed by 1 ml of 6 mol/L hydrochloric acid for 24h at 110℃.Then amino acids was separated,concentrated,evaporated in a vacuum,and derivatized with MBDSTFA,TBDMS-derivatized amino acids can be observed by GC-MS last we get 13C labelling pattern of fifteen aminio acids through mass spectrum.The experimental methods and sample preparation offers referential value for the development of 13C metabolic flux analysis in our courtry.

Quantitative studies of the production phase in rHSA fermentation / 生物工程学报

The model equations of the production phase of rHSA fermentation were derived on the base of both elemental balance and metabolic balance, then the unknown parameters of the model were estimated by multivariable optimization. The possible reasons of discrepancy of production rate between different period of fermentation were discussed. The model could preferably described the relations between different macroscopic reaction rates of the process and keys for the high-efficiency expression of HAS were deduced.

Application of element and metabolism balancing for the cultivation process with Streptomyces aureofaciens / 生物工程学报

On the base of element and metablism balancing, the mathematical model of the cultivation process with Streptomyces aureofaciens was developed, and the unknown parameters in the model were estimated with the method of nonlinear optimization. Firstly the energetic coefficient of CTC biosynthesis was gained, which was 1.8 - 2.8 mol-ATP x C-mol(-1). The macroscopic reaction rates were predicted in the process and compared with the experimental values. The results show that the model can preferably describe the relationships between several macroscopic reaction rates in the process and can supervise the optimization of CTC fermentation process theoretically.

Quantitation & optimization of guanosine fermentation process: prevention of NH4+ accumulation increases guanosine production by 70% / 生物工程学报

Metabolic engineering has become a powerful tool for optimization of industrial fermentation processes. Metabolic engineering usually undergoes three steps: construction of a recombinant strain with improved properties, genetic and biochemical analysis of the strain, and identification of target for further improvement. Metabolic fluxes analysis is an important part of the biochemical analysis. Based on the law of mass conservation and assuming pseudo-steady-state for the intermediates in the metabolic pathways, we have quantitatively analyzed the time course of the flux distribution in Bacillus subtilis and used the data to reveal the nature of the so-called "40 hour" phenomenon in fermentation of guanosine, a key raw material for the synthesis of additives for human consumption and animal feeds. The phenomenon refers to the observation that guanosine production, which proceeds at high rate from 12 hour on, declines around 40 hour while consumption of glucose keeps increasing, leading to the lower yield of the nucleoside. Equations based upon the metabolic network of Bacillus subtilis consisted of EMP pathway, HMP pathway, TCA cycle, oxidative phosphorylation pathway and others reactions of the intermediates, was constructed. The equations were solved by using the quantitative data obtained in this study. The air flow and volume, concentration of oxygen and carbon dioxide in the exit-gas were monitored online; the concentration of biomass, glucose and guanosine was analyzed manually; and the concentration of acetate, citric acid, pyruvate, and 17 amino acids were HPLC quantified. The solutions of the equation were proved to be valid, as the experimental data on oxygen consumption agrees with that of predicted form the equation. The results indicated that at 40h of the fermentation process the flux of HMP pathway, which provides the precursor of the nucleoside, decreased while that of EMP pathway and the pathways that generate amino acids and organic acids increased. The shift correlated with the accumulation of NH4+ in the broth. The assimilation of NH4+ is an energy consuming process and could shift the metabolism to the energy generating EMP pathway. Accordingly, measures were taken to prevent the accumulation of NH4+. The interference indeed stopped the metabolism shift and boosted the guanosine production at 30 g/L, 70% higher than the level reported in literature.

High-density Expression of Recombinant Porcine Insulin Precursor by Pichia pastoris / 微生物学通报

The recombinaut porcine insulin precursor(PIP)produced by Pichia pastoris in shake-flask and 501.fermenter was investigated respectively.The results indicated that 60h induction time length and 2.0%～2.5% methanol addition every day was optimum in shake- flask.The process in 50L fermenter was consisted of batch,feed-batch and induction phases.The relationship between dry cell weight(y) and culture time (t) in growth phase(batch and feed-batch phase)could be described by model y=0.6525e~(0.1907t).Glycerol and ammonia were almost used for cell growth and maintain,and no by-product was observed in batch and fed-batch phase Only 80% ammonia and 70% methanol were used by cell in induction phase.By comparison the results of shake-flask and 50L fermenter,it was concluded that the limit- ing factor in the fermentation of shake-flask and 50L fermenter was dissolved oxygen(DO)and.carbon source,respectively.When scaling the result of shake-flask to 501.fermenter,the control strategy was adapted for 50L fermenter by increasing the feed rate of methanol and the maximum PIP concentration reached 1.72 g/L.