Conversion of corn fiber to ethanol by recombinant E. coli strain FBR3

Escherichia coli strain FBR3 that is an efficient biocatalyst for converting mixed sugar streams (eg, arabinose, glucose, and xylose) into ethanol. In this report, the strain was tested for conversion of corn fiber hydrolysates into ethanol. Corn fiber hydrolysates with total sugar concentrations of 7.5% (w/v) were prepared by reacting corn fiber with dilute sulfuric acid at 145°C. Initial fermentations of the hydrolysate by strain FBR3 had lag times of approximately 30 h judged by ethanol production. Further experiments indicated that the acetate present in the hydrolysate could not solely account for the long lag. The lag phase was greatly reduced by growing the pre-seed and seed cultures on corn fiber hydrolysate. Ethanol yields for the optimized fermentations were 90% of theoretical. Maximum ethanol concentrations were 2.80% w/v, and the fermentations were completed in approximately 50 h. The optimal pH for the fermentation was 6.5. Below this pH, sugar consumption was incomplete and above it, excess base addition was required throughout the fermentation. Two alternative neutralization methods (overliming and overliming with sulfite addition) have been reported for improving the fermentability of lignocellulosic hydrolysates. These methods further reduced the lag phase of the fermentation, albeit by a minor amount. Received 29 September 1998/ Accepted in revised form 20 February 1999     

Kinetics of ethanol production by recombinant Escherichia coli KO11

The fermentation kinetics for separate as well as simultaneous glucose and xylose fermentation with recombinant ethanologenic Escherichia coli KO11 are presented. Glucose and xylose were consumed simultaneously and exhibited mutual inhibition. The glucose exhibited 15 times stronger inhibition in xyclose fermentation than vice versa. The fermentation of condensate from steampretreated willow (Salix) was investigated. The kinetics were studied in detoxified as well as in nondetoxified condensate. The fermentation of the condensate followed two phases: First the glucose and some of the pentoses (xylose in addition to small amounts of arabinose) were fermented simultaneously, and then the remaining part of the pentoses were fermented. The rate of the first phase was independent of the detoxification method used, whereas the rate of the second phase was found to be strongly dependent. When the condensate was detoxified with overliming in combination with sulfite, which was the best detoxification method investigated, the sugars in the condensate, 9 g/L, were fermented in 11 h. The same fermentation took 150 h in nondetoxified condensate. The experimental data were used to develop an empirical model, describing the batch fermentation of recombinant E. coli KO11 in the condensate. The model is based on Monod kinetics including substrate and product inhibition and the sum of the inhibition exerted by the rest of the inhibitors, lumped together. (c) 1995 John Wiley & Sons, Inc.     

A cost effective fermentative production of succinic acid from cane molasses and corn steep liquor by Escherichia coli

AIM: Development and optimization of an efficient and inexpensive medium for succinic acid production by Escherichia coli under anaerobic conditions. METHODS AND RESULTS: Initially, 0.8 gl(-1) of succinic acid was produced in 60 h in 300-ml medium. On optimization, glucose and peptone were replaced by cane molasses and corn steep liquor. Three hundred ml of this medium was inoculated with 4% (v/v) of seed inoculum, incubated at 39 degrees C for 72 h, resulted in 7.1 gl(-1) of succinic acid in 36 h. Scale up in a 10-l fermentor under conditions of controlled pH and continuous CO2 supply in this medium resulted in 17 gl(-1) of succinic acid in 30 h. CONCLUSIONS: A ninefold increase in succinic acid production was obtained in 500-ml anaerobic bottles with optimized medium having cane molasses and corn steep liquor as against initial medium containing glucose and peptone. However, a subsequent scale up in a 10-l fermentor resulted in a 2.5-fold increase in succinic acid production as against optimized medium used in 500-ml anaerobic bottles. SIGNIFICANCE AND IMPACT OF THE STUDY: Succinic acid production was enhanced in medium consisting of inexpensive carbon and nitrogen sources in a shorter span of time.     

利用大肠杆菌工程菌廉价高效生产聚羟基丁酸酯

利用大肠杆菌生产聚羟基脂肪酸酯是近来国际上生物可降解塑料的研究热点,本研究通过对适宜于聚羟基脂肪酸酯生产的大肠杆菌菌株的选择和碳源利用试验,初步确立了大肠杆菌代谢工程改造生产聚羟基脂肪酸酯的基础。并在此基础上,通过对大肠杆菌磷酸烯醇式丙酮酸葡萄糖转移酶系统的改造和工程菌环境诱导系统的应用,解决了大肠杆菌工程菌无法同时利用多种碳源合成聚羟基脂肪酸酯的难题。发酵试验证明,工程化改造的大肠杆菌利用廉价底物在5L发酵罐中分批培养32h后,菌体终浓度能够达到8.24g/L,聚羟基脂肪酸酯占细胞干重的84.6%。     

L-tyrosine production by recombinant Escherichia coli: fermentation optimization and recovery

L-tyrosine (L-tyr) overproducing Escherichia coli strain derived from an L-phenylalanine (L-phe) overproducing strain is characterized in 10 L and 200 L scale fermentations. Deletion of the chromosomal region encoding for the pheA gene, chorismate mutase/prephenate dehydratase, its leader peptide (pheL) and its associated promoter resulted in significant increase in L-tyr production (Olson et al., 2007. Appl Microbiol Biotechnol 74(5):1031-1040). Further increase in titer was achieved by overexpressing tyrA, encoding chorismate mutase/prephenate dehydrogenase, from a strong non-native trc promoter (Olson et al., 2007. Appl Microbiol Biotechnol 74(5):1031-1040). Fermentation optimization studies include media component selection; glucose feed optimization, antifoam agent selection, and understanding fermentation parameters affecting foaming. Generational stability of the strain was evaluated along with rate, titer, and yield of tyrosine formation from glucose. L-tyr titer of 55 g/L in 48 h was demonstrated in 200 L batches, is the highest titer published till date. We have also evaluated two primary separations schemes to isolate and purify L-tyr from the fermentation broth. Physical separation of L-tyr crystals from biomass using a decanter type centrifuge, based on the density difference between the solids, is compared and contrasted with a strategy where L-tyr is first dissolved at pH 11.5 and then acid precipitated from clarified supernatants following removal of biomass using membrane filtration. L-tyr product purity of 98% with yields ranging from 90% to 95% is demonstrated.     

循环利用重组大肠杆菌细胞转化合成丁二酸

研究了回收丁二酸发酵液中的大肠杆菌进行细胞转化的可行性,以转化率和生产效率为指标,考察了不同菌体浓度、底物浓度、pH调节剂对细胞转化的影响。发酵结果表明大肠杆菌可以在仅含有葡萄糖和pH调节剂的水环境中转化生产丁二酸,并确定了最佳的转化条件为:细胞浓度(OD600)50,底物浓度40g/L,缓冲盐为MgCO3。基于优化好的条件,在7L发酵罐中进行重复批次转化,第1次转化的转化率和生产效率分别达到91%和3.22g/(L·h),第2次转化的生产效率和转化率达到了86%和2.04g/(L·h),第3次转化的转化率和生产效率分别达到了83%和1.82g/(L·h)。     

Parametric studies of ethanol production form xylose and other sugars by recombinant Escherichia coli

The conversion of xylose to ethanol by recombinant Escherichia coli has been investigated in pH-controlled batch fermentations. Chemical and environmental parameters were varied to determine tolerance and to define optimal conditions. Relatively high concentrations of ethanol (56 g/L) were produced from xylose with excellent efficiencies. Volumetric productivities of up to 1.4 g ethanol/L h were obtained. Productivities, yields, and final ethanol concentrations achieved from xylose with recombinant E. coli exceeded the reported values with other organisms. In addition to xylose, all other sugar constituents of biomass (glucose, mannose, arabinose, and galactose) were efficiently converted to ethanol by recombinant E. coli. Unusually low inocula equivalent to 0.033 mg of dry cell weight/L were adequate for batch fermentations. The addition of small amounts of calcium, magnesium, and ferrous ions stimulated fermentation. The inhibitory effects of toxic compounds (salts, furfural, and acetate) which are present in hemicellulose hydrolysates were also examined.     

Succinate production from sucrose by metabolic engineered Escherichia coli strains under aerobic conditions

Two metabolically engineered E. coli strains HL2765k and HL27659k, while capable of producing succinate from glucose with high yields, are not able to grow and produce succinate on sucrose. Consequently, the pUR400 plasmid containing scrK, Y, A, B, and R genes was introduced into HL2765k and HL27659k, respectively. Shake flask culture studies showed that the resulting strains can utilize sucrose; the strain HL2765k pUR400 and HL27659k pUR400 can produce succinate aerobically with a molar yield of 0.78 ± 0.02 mol/mol and 1.35 ± 0.13 mol/mol, respectively. On introduction of the plasmid pHL413, which encodes the heterologous pyruvate carboxylase (PYC) from Lactococcus lactis, the molar succinate yield increased to 1.60 ± 0.01 mol of succinate per mole of sucrose by the HL2765k pUR400 pHL413 strain and to 1.84 ± 0.10 by the HL27659k pUR400 pHL413 strain. In aerobic batch bioreactor studies, the succinate production rate was faster, and succinate production reached 101.83 mM with a yield of 1.90 when dissolved oxygen (DO) was controlled at 40 ± 7%. In addition, the results showed that DO had an important effect on succinate production by influencing PYC activity. This work demonstrates the possibility of producing succinate aerobically using sucrose as the carbon source.     

Eliminating side products and increasing succinate yields in engineered strains of Escherichia coli C

Derivatives of Escherichia coli C were previously described for succinate production by combining the deletion of genes that disrupt fermentation pathways for alternative products (ldhA::FRT, adhE::FRT, ackA::FRT, focA-pflB::FRT, mgsA, poxB) with growth-based selection for increased ATP production. The resulting strain, KJ073, produced 1.2 mol of succinate per mol glucose in mineral salts medium with acetate, malate, and pyruvate as significant co-products. KJ073 has been further improved by removing residual recombinase sites (FRT sites) from the chromosomal regions of gene deletion to create a strain devoid of foreign DNA, strain KJ091(DeltaldhA DeltaadhE DeltaackA DeltafocA-pflB DeltamgsA DeltapoxB). KJ091 was further engineered for improvements in succinate production. Deletion of the threonine decarboxylase (tdcD; acetate kinase homologue) and 2-ketobutyrate formate-lyase (tdcE; pyruvate formate-lyase homologue) reduced the acetate level by 50% and increased succinate yield (1.3 mol mol(-1) glucose) by almost 10% as compared to KJ091 and KJ073. Deletion of two genes involved in oxaloacetate metabolism, aspartate aminotransferase (aspC) and the NAD(+)-linked malic enzyme (sfcA) (KJ122) significantly increased succinate yield (1.5 mol mol(-1) glucose), succinate titer (700 mM), and average volumetric productivity (0.9 g L(-1) h(-1)). Residual pyruvate and acetate were substantially reduced by further deletion of pta encoding phosphotransacetylase to produce KJ134 (DeltaldhA DeltaadhE DeltafocA-pflB DeltamgsA DeltapoxB DeltatdcDE DeltacitF DeltaaspC DeltasfcA Deltapta-ackA). Strains KJ122 and KJ134 produced near theoretical yields of succinate during simple, anaerobic, batch fermentations using mineral salts medium. Both may be useful as biocatalysts for the commercial production of succinate.     

Ethanol production from corn cob hydrolysates by <Emphasis Type="Italic">Escherichia coli</Emphasis> KO11

Corn cob hydrolysates, with xylose as the dominant sugar, were fermented to ethanol by recombinant Escherichia coli KO11. When inoculum was grown on LB medium containing glucose, fermentation of the hydrolysate was completed in 163 h and ethanol yield was 0.50 g ethanol/g sugar. When inoculum was grown on xylose, ethanol yield dropped, but fermentation was faster (113 h). Hydrolysate containing 72.0 g/l xylose and supplemented with 20.0 g/l rice bran was readily fermented, producing 36.0 g/l ethanol within 70 h. Maximum ethanol concentrations were not higher for fermentations using higher cellular concentration inocula. A simulation of an industrial process integrating pentose fermentation by E. coli and hexose fermentation by yeast was carried out. At the first step, E. coli fermented the hydrolysate containing 85.0 g/l xylose, producing 40.0 g/l ethanol in 94 h. Baker's yeast and sucrose (150.0 g/l) were then added to the spent fermentation broth. After 8 h of yeast fermentation, the ethanol concentration reached 104.0 g/l. This two-stage fermentation can render the bioconversion of lignocellulose to ethanol more attractive due to increased final alcohol concentration. Journal of Industrial Microbiology & Biotechnology (2002) 29, 124–128 doi:10.1038/sj.jim.7000287 Received 20 February 2002/ Accepted in revised form 04 June 2002     

重组基因表达对大肠杆菌生理的影响

重组基因在表达外源蛋白质时常常会耗用大量的宿主细胞资源,从而对宿主造成代谢负荷,代谢负荷使得宿主的生化和生理产生很大的变化,甚至损害宿主正常的代谢功能。而过重的代谢负荷会影响目标蛋白的表达量和表达质量。综述了产生代谢负荷的原因,宿主细胞对代谢负荷的应激反应、以及减轻代谢负荷的策略。     

产琥珀酸工程菌株的发酵工艺条件优化

对实验室构建的产琥珀酸大肠杆菌工程菌株(E.coliQZ1111)进行发酵工艺条件研究。以AM1低盐培养基为基础,研究不同C、N源及其质量浓度,培养基初始pH和发酵温度等因素对琥珀酸的影响,并在5L发酵罐中进行了补料-分批发酵实验。优化后的发酵条件为葡萄糖20g/L,玉米浆10g/L,pH6.4,发酵温度37℃。在5L发酵罐中培养,琥珀酸产量达到47.9g/L。     

Vgb在大肠埃希菌中表达及生物活性的研究

目的将vgb克隆到大肠埃希菌表达载体pQE-30中,研究vgb表达产物对细胞摄氧能力的影响。方法利用PCR和基因重组技术克隆vgb与大肠埃希菌表达质粒pQE V,大肠埃希菌转化采用CaCl2法,VHb活性分析采用CO示差光谱法。结果克隆了vgb和重组质粒pQE V,vgb基因在大肠埃希菌中获得表达,在A420 nm处达到典型吸收峰。结论 vgb在大肠埃希菌中表达产物加强了对氧的摄取能力,对解决细胞高密度发酵培养中氧需矛盾、促进代谢产物的产率具有非常重要的应用价值。     

大肠杆菌K88菌毛蛋白发酵工艺的初步研究

采用液体培养基包括牛肉膏蛋白胨培养基和强化营养肉汤培养基对大肠杆菌K88进行发酵培养,采用不同摇瓶培养时间和不同pH值的培养基观察发酵结果,研究菌体和菌毛生产量的相关性,并通过紫外分光光度计UV751于600nm处测量菌体OD值以对菌种发酵情况进行检测.热激分离菌体和菌毛蛋白,(NH4)2SO4盐析分离纯化K88菌毛蛋白并用分光光度计于280nm处测定其OD值.透析后经SDSP-AGE检测菌毛蛋白纯度.根据实验结果优化发酵培养条件,确定菌种的最佳发酵工艺,以收获最多的K88菌毛蛋白.经过实验研究,最终确定了大肠杆菌K88在pH值为6.5、转速为250r/min的条件下发酵18个h,菌体和菌毛生产量均达到高峰,同时得出菌毛蛋白和菌体成正相关.     

Virulence-related DNA sequences and adherence patterns in strains of enteropathogenic Escherichia coli

The presence of the genes for Escherichia coli adherence factor (EAF), attaching and effacing lesion (eae) and bundle-forming pili (bfp) in 72 strains identified as enteropathogenic E. coli (EPEC) by slide agglutination was evaluated using hybridization and PCR. The adherence property of these strains was assayed using 3h HeLa cells adherence assay. The results obtained indicated that virulence-associated genes were present in 65% of the strains but only ten (13.9%) isolates were positive for all the three markers (typical EPEC), 37 (51.4%) isolates carried either one or two of these determinants (atypical EPEC) and the remaining 25 (34.7%) were negative for all these genes. In vitro adherence assay showed that 44 (61.1%) strains adhered to HeLa cells with a defined pattern, 13 (18.1%) isolates adhered loosely with no definite pattern and the remaining 15 (20.8%) were non-adherent. Analysis of the results showed a statistically significant association between the presence of the virulence-related genes with adherence of the strains with a defined pattern (P相似文献   

Closed-loop control of fed-batch cultures of recombinant Escherichia coli using on-line HPLC

This article describes a fully automated system for the on-line monitoring and closed-loop control of a fed-batch fermentation of recombinant Escherichia coli, and presents two case studies of its used in limiting production of unwanted byproducts such as acetic in fed-batch fermentations. The system had two components. The first components, on-line monitoring, comprised an aseptic sampling device, a microcentrifuge, and HPLC System. These instruments removed a Sample from a fermentor, spun it at high speed to separate solid and liquid components, and then automatically injected the supernatant onto an HPLC column for analysis. The second component consisted of control algorithms programmed using the LabView visual programming environment in a control computer that was linked via a remote components were linked so that results from the on-line HPLC were captured and used by the control algorithm was designed to demonstrate coarse feedback control to confirm the operability of the controller. The second case study showed how the system could be used in a more sophisticated feedings strategy providing fine control and limiting acetate concentration to a low level throughout the fermentation. (c) 1994 John Wiley & Sons, Inc.     

Physiological effects of TGF(alpha)-PE40 expression in recombinant Escherichia coli JM109

Physiological effects of isopropyl-thiogalactopyranoside (IPTG) induction were examined in Escherichia coli strain JM109 expressing a fusion protein composed of transforming growth factor alpha and a 40-kD portion of Pseudomonas aeruginosa exotoxin A (TGF(alpha)-PE40) under control of the tac promoter. Fermentations at the 15-L scale in complex medium compared growth and metabolite profiles of the untransformed JM109 host strain, the strain transformed with the vector lacking the TGF(alpha)-PE40 open reading frame (JM109[pKK2.7]), and the strain with the complete plasmid for TGF(alpha)-PE40 expression (JM109[pTAC-TGF57-PE40]). Metabolite and growth profiles of JM109 (pTAC-TGF57-PE40) cultures changed significantly in IPTG-induced versus uninduced cultures. Prior to induction, glucose was metabolized to acetate or completely oxidized to CO(2). Following induction, pyruvate was also excreted in addition to acetate. In the absence of inducer, pyruvate was excreted by JM109 (pTAC-TGF57-PE40) only when dissolved oxygen levels fell to less than 10% of saturation (microaerobic rather than anaerobic conditions). The untransformed JM109 host strain or JM109 (pKK2.7) did not excrete pyruvate in the presence or absence of inducer, although JM109 (pKK2.7) exhibited a pattern of growth following addition of IPTG that closely resembled JM109 (pTAC-TFG57-PE40). Fermentations of JM109 (pTAC-TFG57-PE40) in a synthetic medium supported lower expression levels, but resulted in similar alterations in metabolite profiles. Induction in synthetic medium resulted in pyruvate excretion without further acetate accumulation. Taken together, these data suggest that one consequence of TGF(alpha)-PE40 expression in JM109 is altered patterns of pyruvate oxidation. (c) 1992 John Wiley & Sons, Inc.     

Overproduction of a Clostridium cellulolyticum endoglucanase by mutant strains of Escherichia coli

We have studied the expression of an endoglucanase from Clostridium cellulolyticum in mutant strains of Escherichia coli that overproduce haemolysin. When these mutants were transformed with plasmids encoding the endoglucanase, they showed a significantly enhanced endoglucanase activity, compared to transformed parental strains. Among the mutants, strain Hha-2 showed the highest production. We have identified the endoglucanase gene product synthesized in E. coli Hha-2/pBP8 and detected an increased amount of the enzyme parallel to the increase of endoglucanase activity. This was mainly localized in the periplasm and only a small percentage of it was found in the culture fluid.     

重组大肠杆菌右旋糖酐蔗糖酶的纯化及其性质

[目的]研究工程菌E.coli BL21(DE3)/pET28-dexYG产右旋糖酐蔗糖酶的纯化和酶学性质.[方法]工程菌经过IPTG诱导后生产含His-tag融合蛋白的右旋糖酐蔗糖酶,通过硫酸铵沉淀、Ni-NTA亲和层析纯化,得到纯度较高的酶蛋白,并对纯酶进行了酶学性质及动力学研究.[结果]经过SDS-PAGE测得该酶的分子量约为170 kDa,与理论推测值基本相同.以蔗糖为底物,酶促反应的最适温度为25～30℃,最适pH值为5.4,动力学常数Km值为10.43 mmol/L;酶活在pH 5.0～8.0较为稳定,在室温(25 ℃)保藏4天仍有59%的酶活力,4℃保存7周酶活力仅下降一半,但在35℃以上失活很快;Ca2 对催化作用有较大的促进,Mg2 有微弱的促进作用,K 对催化反应无影响,Cu2 的抑制作用最强.其他试剂对重组酶的活性有不同程度的影响,其中SDS抑制作用很强.[结论]研究为重组右旋糖酐蔗糖酶纯酶的获取、得到稳定性好、活性高的酶反应体系及利用该酶进行催化反应和工业化应用提供了重要参数.     

Effects of ethanol on the growth and elongation of Escherichia coli under high pressures up to 40 MPa

The effects of ethanol on growth, viability and cell length were studied in Escherichia coli cultured under pressures up to 40 MPa (400 bar). A pressure of 10 MPa reversed the effect of ethanol in retarding cell growth. Cells cultured in the absence of ethanol became about seven times longer at 40 MPa than at atmospheric pressure, and some cells showed incomplete cell division. Ethanol also increased cell length but these effects were not seen at pressures of 20 MPa or more.