高强度酒精连续发酵

从多株酒精酵母菌株中筛选出S.cerevisiaeKG作为酒精生产菌株。该菌株具有较好的酒精发酵活力和絮凝性。使用具有细胞循环的连续发酵双罐系统,酒精生产强度达到30.5（g／1.h）。根据该系统的动力学模型,讨论了获得高强度酒精连续发酵的途径。     

Fermentation Kinetics and Continuous Process of L-Asparaginase Production

For the purpose of obtaining L-asparaginase in quantities from Erwinia aroideae, cell growth and enzyme formation were investigated in both batch and continuous fermentation. Using yeast extract as a growth-limiting substrate, the relationship between specific growth rate and substrate concentration was found to fit the Monod equation. The optimum temperature for enzyme production was 24 C, although cell growth was higher at 28 C. The enzyme yield reached its maximum of 4 IU/ml during the negative acceleration growth phase which occurs just prior to stationary growth. Compared to batch fermentations, the continuous fermentation process gave a lower enzyme yield except when the fermentation was conducted at a dilution rate of 0.1 hr(-1). The graphical method frequently used for prediction of continuous fermentation does not apply to L-asparaginase production by E. aroideae. The optimum temperature for enzyme production in continuous process was 24 C, which was the same as in batch process. Increasing the temperature from 24 to 28 C resulted in a 20% loss of enzyme yield.     

Continuous Cellulosic Bioethanol Fermentation by Cyclic Fed-Batch Cocultivation

Cocultivation of cellulolytic and saccharolytic microbial populations is a promising strategy to improve bioethanol production from the fermentation of recalcitrant cellulosic materials. Earlier studies have demonstrated the effectiveness of cocultivation in enhancing ethanolic fermentation of cellulose in batch fermentation. To further enhance process efficiency, a semicontinuous cyclic fed-batch fermentor configuration was evaluated for its potential in enhancing the efficiency of cellulose fermentation using cocultivation. Cocultures of cellulolytic Clostridium thermocellum LQRI and saccharolytic Thermoanaerobacter pseudethanolicus strain X514 were tested in the semicontinuous fermentor as a model system. Initial cellulose concentration and pH were identified as the key process parameters controlling cellulose fermentation performance in the fixed-volume cyclic fed-batch coculture system. At an initial cellulose concentration of 40 g liter⁻¹, the concentration of ethanol produced with pH control was 4.5-fold higher than that without pH control. It was also found that efficient cellulosic bioethanol production by cocultivation was sustained in the semicontinuous configuration, with bioethanol production reaching 474 mM in 96 h with an initial cellulose concentration of 80 g liter⁻¹ and pH controlled at 6.5 to 6.8. These results suggested the advantages of the cyclic fed-batch process for cellulosic bioethanol fermentation by the cocultures.     

Continuous Fermentation in high flow rate fermenter systems

In commercial batch processes the productivity of product formation is low. But a significant increase of productivity can be achieved in continuous fermentations. By using high flow rate fermenter systems characterized by a relatively long retention time of biomass in comparison with the retention time of the liquid we can realize a high-performance fermentation. The problem of holding back the biomass within the reactor could be solved by means of membranes being impenetrable to the cells, but permeable to the hydraulic phase. Such a process technology was successfully tested for its applicability in alcoholic and lactic acid fermentations. The maximum productivities obtained on this way were ? = 120 g/l. · h for ethanol production and ? = 51 g/l. h for lactic acid fermentation, respectively.     

Membrane-Integrated Fermentation System for Improving the Optical Purity of D-Lactic Acid Produced during Continuous Fermentation

This report describes the production of highly optically pure D-lactic acid by the continuous fermentation of Sporolactobacillus laevolacticus and S. inulinus, using a membrane-integrated fermentation (MFR) system. The optical purity of D-lactic acid produced by the continuous fermentation system was greater than that produced by batch fermentation; the maximum value for the optical purity of D-lactic acid reached 99.8% enantiomeric excess by continuous fermentation when S. leavolacticus was used. The volumetric productivity of the optically pure D-lactic acid was about 12 g/L/h, this being approximately 11-fold higher than that obtained by batch fermentation. An enzymatic analysis indicated that both S. laevolacticus and S. inulinus could convert L-lactic acid to D-lactic acid by isomerization after the late-log phase. These results provide evidence for an effective bio-process to produce D-lactic acid of greater optical purity than has conventionally been achieved to date.     

微生物连续发酵酶催化动力系统的鲁棒性与并行计算

依据甘油连续发酵生产1,3-丙二醇的非线性酶催化动力系统.针对1,3-丙二醇可能存在的跨膜运输方式建立相应的动力学模型,提出了酶催化动力系统的定量鲁棒性定义,并建立了以鲁棒性为性能指标、非线性动力系统为主要约束的参数辨识模型.由于求解该辨识问题的数值计算量大,在普通的PC机上难以完成,因此本文构建了相应的并行算法.根据数值结果推断出1,3-丙二醇最有可能的跨膜运输方式,这对于进一步研究甘油连续发酵的机理具有重要的参考价值.     

Kinetics of Insoluble Cellulose Fermentation by Continuous Cultures of Ruminococcus albus

Data from analyses of continuous culture fermentation of insoluble cellulose by Ruminococcus albus 7 were used to derive constants for the rate of cellulose hydrolysis and fermentation, growth yield, and maintenance. Cellulose concentration was 1% in the nutrient reservoir, and hydraulic retention times of 0.5, 1.0, 1.5, 1.75, and 2.0 days were used. Concentrations of reducing sugars in the cultures were negligible (less than 1%) compared with the amount of hydrolyzed cellulose, indicating that cellulose hydrolysis was the rate-limiting step of the fermentation. The rate of utilization of cellulose depended on the steady-state concentration of cellulose and was first order with a rate constant (k) of 1.18 day⁻¹. The true microbial growth yield (Y) was 0.11 g g⁻¹, the maintenance coefficient (m) was 0.10 g g⁻¹ h⁻¹, and the maximum Y_ATP was 7.7 g of biomass (dry weight) mol of ATP⁻¹.     

Novobiocin analogues with second-generation noviose surrogates

Hsp90 is a promising therapeutic target for the treatment of cancer. Novobiocin is the first Hsp90 C-terminal inhibitor ever identified and recent structure–activity relationship studies on the noviose sugar identified several commercially available amines as suitable surrogates. In an effort to further understand this region of the molecule, analogues containing various N′-amino substituents were prepared and evaluated against two breast cancer cell lines for determination of their efficacy. Compound 37j manifested the most potent anti-proliferative activity from these studies and induced Hsp90-dependent client protein degradation at mid nano-molar concentrations.     

Mode of Action of Novobiocin in Escherichia coli

The mechanism of action of novobiocin was studied in various strains of Escherichia coli. In all strains tested except mutants of strain ML, the drug immediately and reversibly inhibited cell division, and later slowed cell growth. The previously described impairment of membrane integrity, degradation of ribonucleic acid (RNA), and associated bactericidal effect were found to be peculiar to ML strains. The earliest and greatest effect in all strains was an inhibition of deoxyribonucleic acid (DNA) synthesis; RNA synthesis was inhibited to a lesser extent, and cell wall and protein synthesis were affected later. The inhibition of nucleic acid synthesis was accompanied by an approximately threefold accumulation of all eight nucleoside triphosphates. Since novobiocin does not inhibit nucleoside triphosphate synthesis, degrade DNA, or immediately affect energy metabolism, it must inhibit the synthesis of DNA and RNA by direct action on template-polymerase complexes.     

Copper Sulfate-induced Fermentation Changes in Continuous Cultures of the Rumen Microbial Ecosystem

The effect of CuSO(4) on fermentation was studied in a continuously cultured rumen ecosystem. CuSO(4), introduced at a level of 50 mg/500 ml of culture volume twice daily, caused a marked inhibition of fermentation of concentrates. Fermentation of alfalfa hay was not inhibited by the same CuSO(4) concentration when the inoculum for the culture was obtained from a cow maintained on a normal concentrate ration. When the inoculum was from a cow on a high concentrate ration, hay fermentation was partially inhibited by CuSO(4). Concentrations of CuSO(4) that did not inhibit the fermentation of alfalfa hay or hay-concentrate mixtures caused preferential production of propionic acid and decreased production of methane.     

Fermentation of Cellulosic Substrates in Batch and Continuous Culture by Clostridium thermocellum

Fermentation of dilute-acid-pretreated mixed hardwood and Avicel by Clostridium thermocellum was compared in batch and continuous cultures. Maximum specific growth rates per hour obtained on cellulosic substrates were 0.1 in batch culture and >0.13 in continuous culture. Cell yields (grams of cells per gram of substrate) in batch culture were 0.17 for pretreated wood and 0.15 for Avicel. Ethanol and acetate were the main products observed under all conditions. Ethanol:acetate ratios (in grams) were approximately 1.8:1 in batch culture and generally slightly less than 1:1 in continuous culture. Utilization of cellulosic substrates was essentially complete in batch culture. A prolonged lag phase was initially observed in batch culture on pretreated wood; the length of the lag phase could be shortened by addition of cell-free spent medium. In continuous culture with ~5 g of glucose equivalent per liter in the feed, substrate conversion relative to theoretical ranged from 0.86 at a dilution rate (D) of 0.05/h to 0.48 at a D of 0.167/h for Avicel and from 0.75 at a D of 0.05/h to 0.43 at a D of 0.11/h for pretreated wood. At feed concentrations of <4.5 g of glucose equivalent per liter, conversion of pretreated wood was 80 to 90% at D = 0.083/h. Lower conversion was obtained at higher feed substrate concentrations, consistent with a limiting factor other than cellulose. Free Avicelase activities of 12 to 84 mU/ml were observed, with activity increasing in this order: batch cellobiose, batch pretreated wood < batch Avicel, continuous pretreated wood < continuous Avicel. Free cellulase activity was higher at increasing extents of substrate utilization for both pretreated wood and Avicel under all conditions tested. The results indicate that fermentation parameters, with the exception of free cellulase activity, are essentially the same for pretreated mixed hardwood and Avicel under a variety of conditions. Hydrolysis yields obtained with C. thermocellum cellulase acting either in vitro or in vivo were comparable to those previously reported for Trichoderma reesei on the same substrates.     

Novobiocin inhibits the SV40 enhancer activity

Using a transient expression assay, we have analysed the effect of novobiocin, DNA topoisomerase II inhibitor, on simian virus 40(SV40) enhancer activities. We used the recombinant clones containing type I or II collagen promoters placed upstream of the bacterial chloramphenicol acetyltransferase (CAT) gene with or without SV40 enhancer. We observed the expected increase in CAT activities due to the presence of the SV40 enhancer. Interestingly, CAT gene expression of the enhancer-containing constructs were inhibited more sensitively by novobiocin than that of the enhancer-less construct. This findings lead us propose that DNA superhelicity mediated by topoisomeraseII is one of the important factor for the manifestation of SV40 enhancer activity.     

Novobiocin inhibits passive chromatin assembly in vitro.

Novobiocin, an inhibitor of prokaryotic DNA gyrase and eukaryotic type II topoisomerase enzymes, interferes with in vitro chromatin assembly using purified histones, DNA and nucleoplasmin. The target of inhibition is not topoisomerase II; this energy-independent assembly system lacks any ATP and Mg2+-dependent type II topoisomerase or gyrase activities. Rather, novobiocin interacts with histones, disrupting histone-histone associations required for octamer formation, and causing histones to precipitate from both nucleoplasmin-histone and histone-DNA complexes. Thus, novobiocin is able to generate 'dynamic' chromatin in vitro in the absence of ATP and Mg2+ by removing histones from previously assembled static chromatin, so that the DNA supercoils, previously constrained by conventional nucleosomes, become susceptible to removal by topoisomerase I.     

Improved Bioreaction Kinetics for the Simulation of Continuous Ethanol Fermentation by Saccharomyces cerevisiae

A kinetic model for the production of ethanol by Saccharomyces cerevisiae has been developed from semiempirical analysis. The values for the parameters in this model were then determined by nonlinear multiple regression using the data of Bazua and Wilke ( 1977). The final equations were μ=0.427s(1-(p/101.6)^1.95)/(0.245+s), Y_X/p=0.291, and Y_X/s=0.152(1-p/302.3). This model was then used to simulate a continuous stirred tank fermentor (CSTF) and compared to other models using the same experimental data but different kinetics. The equations required to use these kinetics in a CSTF with recycle were then developed. From this simulation, it was found that, for a CSTF with recycle, the best configuration to operate is an external recycle, with a low bleed and recycle ratio.