响应面法优化重组大肠杆菌产蔗糖异构酶发酵培养基

通过碳氮源的不同浓度对重组大肠杆菌E.coil BL21(DE3)发酵产蔗糖异构酶(SIase)的影响,并借助于数学分析软件Design Expert,结合Plackett-Burman试验设计和中心复合试验设计分析法,对蔗糖异构酶的产生菌进行了发酵培养基的优化研究。实验表明,最佳培养基组分为甘蔗糖蜜10.65 g/L,玉米浆22.22 g/L,NaCl 7.57 g/L ,MgSO₄·7H₂O 0.52 g/L, KH₂PO₄ 4.46g/L,优化后的蔗糖异构酶活力达到29.1U/ml,比LB培养基培养重组大肠杆菌(15U/ml),蔗糖异构酶活力提高了94%,与原始菌大黄欧文菌NX-5相比提高了21.4倍(1.3U/ml)。     

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)。     

碳源对重组大肠杆菌两阶段发酵产丁二酸的影响

研究了在好氧培养基中分别添加不同碳源对两阶段发酵菌体生长、酶活及代谢产物分布的影响,结果表明添加4mmol/L葡萄糖和12,54,80mmol/L乙酸钠均可以提高好氧阶段的菌体密度和相关酶活。将不同条件下培养的菌体转接厌氧发酵后,厌氧阶段的酶活和代谢产物分布也发生改变。进一步对酶活及代谢产物分析表明：Escherichia coli NZN111(sfcA)厌氧发酵过程中,磷酸烯醇式丙酮酸羧化激酶(PCK)是产丁二酸的关键酶,丙酮酸激酶(PYK)主要和副产物丙酮酸的积累有关,异柠檬酸裂解酶(ICL)对丁二酸产量也有一定影响。好氧培养基中添加80mmol/L乙酸钠,厌氧发酵结束时丁二酸的质量收率可达89.0%,相比对照提高了16.6%。     

以蔗糖为底物利用重组大肠杆菌合成甘露醇

【目的】异型发酵乳酸菌可利用胞内产生的甘露醇脱氢酶将果糖高效转化为甘露醇,但果糖作为底物相对昂贵,不利于工业化生产。为了降低生产成本,必须选择廉价的底物。蔗糖相对便宜,并且大量存在于自然界中,能够被重组大肠杆菌利用产生甘露醇。蔗糖水解酶(Sucrose hydrolase)和甘露醇脱氢酶(Mannitol dehydrogenase)是发酵生产甘露醇中催化蔗糖转化成甘露醇的关键酶,构建蔗糖水解酶和甘露醇脱氢酶共表达菌株并进行相关研究是本文的主旨。【方法】利用PCR方法分别从植物乳杆菌(Lactobacillus plantarum)和布氏乳杆菌(Lactobacillus buchneri)基因组DNA中获得sac A和mdh基因,得到大小分别为1 502 bp和1 032 bp的目的基因,经序列分析后将其连接到表达载体p ET-28a(+)上,得到重组表达载体p ET28a-sac A-mdh。将重组质粒转化到大肠杆菌BL21(DE3)中,并用SDS-PAGE分析目的蛋白的表达情况并测定其酶活。【结果】SDS-PAGE显示表达蛋白的大小亚基分子量分别为55.1 k D和37.8 k D,与预期分子量一致,实现sac A和mdh基因的表达。蔗糖水解酶和甘露醇脱氢酶酶活分别为25.78 U/m L和14.56 U/m L。对重组菌株BL21(DE3)/p ET28a-sac A-mdh进行发酵条件优化,甘露醇质量浓度达到45.19 g/L,总糖转化率为37.66%。【结论】与乳酸菌利用蔗糖发酵生产甘露醇相比,产量提高了6倍,且具有发酵周期短、稳定性高等优点,菌株的成功构建为甘露醇工业化生产奠定了基础。     

过量表达苹果酸脱氢酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111是敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸-甲酸裂解酶的编码基因 (pflB) 的工程菌,厌氧条件下由于辅酶NAD(H) 的不平衡导致其丧失了代谢葡萄糖的能力。构建了苹果酸脱氢酶的重组菌大肠杆菌NZN111/pTrc99a-mdh,在厌氧摇瓶发酵过程中通过0.3 mmol/L的IPTG诱导后重组菌的苹果酸脱氢酶 (Malate dehydrogenase,MDH) 酶活较出发菌株提高了14.8倍,NADH/NAD+的比例从0.64下降到0.26,同时NAD+和NADH浓度分别     

固定化黑曲霉利用糖蜜发酵生产柠檬酸

利用海藻酸钙凝胶包埋黑曲霉W1-2的孢子及菌丝体,制成的固定化细胞经预培养后,用于发酵糖蜜制取柠檬酸。确定了固定化细胞摇瓶发酵生产柠檬酸的最佳条件:糖蜜浓度12%。初始pH值4.0,培养温度30℃等。在此条件下发酵12天,柠檬酸浓度达39 g/L。对分批发酵生产柠檬酸进行了初步研究。     

大肠杆菌AFP111菌体回收连续转化生产丁二酸

在利用大肠杆菌AFP111厌氧发酵生产丁二酸过程中,随着产物丁二酸的不断积累,菌体活力和产酸能力逐渐降低,而通过回收菌体在新鲜培养基中重复发酵,可延长厌氧发酵时间,但是丁二酸生产效率较低。为了提高菌体回收丁二酸的转化效率,通过在回收菌体时有氧诱导 3 h,以纯水为培养基,进行丁二酸转化发酵。在连续进行 3 批次的发酵后,丁二酸的总产量和最终收率分别为 56.50 g/L和90%,生产速率达到了 0.81 g/(L·h),比未诱导情况下的生产速率提高了13%。     

基于辅因子调控对大肠杆菌两阶段发酵产丁二酸的影响

考察了E.coli NZN111及其重组菌株E.coli NZN111/pTrc99a-pncB发酵生产丁二酸的性能。E.coli NZN111两阶段发酵丁二酸的同时,会造成丙酮酸的大量积累。研究发现:通过过量表达烟酸转磷酸核糖激酶,两阶段发酵重组菌株E.coli NZN111/pTrc99a-pncB,减少丙酮酸的积累且无副产物乙酸生成,提高丁二酸的产量,丁二酸得率和耗糖速率分别提高了139%和20%。     

利用甜菜糖蜜补料发酵生产丁醇

从土壤中分离出1株适合利用甜菜糖蜜发酵生产丁醇的丙酮丁醇梭菌(Clostridium acetobutylicum)2N,通过优化发酵条件,得到最适发酵温度为33℃,玉米浆最适添加量为15g/L,发现甜菜糖蜜中还原糖质量浓度高于50g/L时影响菌株的生长和溶剂生产。以补料分批发酵方式降低底物抑制,33℃发酵48h后,丁醇和总溶剂的质量浓度分别达到14.15g/L和19.65g/L,丁醇质量分数超过70%。     

过量表达烟酸转磷酸核糖激酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111厌氧发酵的主要产物为丁二酸,是发酵生产丁二酸的潜力菌株。但是由于敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸甲酸裂解酶的编码基因 (pflB),导致辅酶NADH/NAD+不平衡,厌氧条件下不能利用葡萄糖生长代谢。构建烟酸转磷酸核糖激酶的重组菌Escherichia coli NZN111/pTrc99a-pncB,在厌氧摇瓶发酵过程中通过添加0.5 mmol/L的烟酸、0.3 mmol/L的IPTG诱导后重组菌的烟酸转磷酸核糖激酶 (Nicotinic acid phosphor     

Production of succinic acid from sucrose and sugarcane molasses by metabolically engineered Escherichia coli

Sucrose-utilizing genes (cscKB and cscA) from Escherichia coli KO11 were cloned and expressed in a metabolically engineered E. coli KJ122 to enhance succinate production from sucrose. KJ122 harboring a recombinant plasmid, pKJSUC, was screened for the efficient sucrose utilization by growth-based selection and adaptation. KJ122-pKJSUC-24T efficiently utilized sucrose in a low-cost medium to produce high succinate concentration with less accumulation of by-products. Succinate concentrations of 51 g/L (productivity equal to 1.05 g/L/h) were produced from sucrose in anaerobic bottles, and concentrations of 47 g/L were produced in 10 L bioreactor within 48 h. Antibiotics had no effect on the succinate production by KJ122-pKJSUC-24T. In addition, succinate concentrations of 62 g/L were produced from sugarcane molasses in anaerobic bottles, and concentrations of 56 g/L in 10 L bioreactor within 72 h. These results demonstrated that KJ122-pKJSUC-24T would be a potential strain for bio-based succinate production from sucrose and sugarcane molasses.     

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.     

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.     

Production of p-Aminobenzoic acid by metabolically engineered Escherichia coli

The production of chemical compounds from renewable resources is an important issue in building a sustainable society. In this study, Escherichia coli was metabolically engineered by introducing T7lac promoter-controlled aroF^fbr, pabA, pabB, and pabC genes into the chromosome to overproduce para-aminobenzoic acid (PABA) from glucose. Elevating the copy number of chromosomal P_T7lac-pabA-pabB distinctly increased the PABA titer, indicating that elevation of 4-amino-4-deoxychorismic acid synthesis is a significant factor in PABA production. The introduction of a counterpart derived from Corynebacterium efficiens, pabAB (ce), encoding a fused PabA and PabB protein, resulted in a considerable increase in the PABA titer. The introduction of more than two copies of P_T7lac-pabAB (ce-mod), a codon-optimized pabAB (ce), into the chromosome of a strain that simultaneously overexpressed aroF^fbr and pabC resulted in 5.1?mM PABA from 55.6?mM glucose (yield 9.2%). The generated strain produced 35?mM (4.8?g?L^?1) PABA from 167?mM glucose (yield 21.0%) in fed-batch culture.     

代谢工程大肠杆菌利用甘油高效合成L-乳酸

以甘油为碳源高效合成L-乳酸有助于推进油脂水解产业和生物可降解材料制造业的共同发展。为此,首先分别从凝结芽胞杆菌Bacillus coagulans CICIM B1821和大肠杆菌Escherichia coli CICIM B0013中克隆了L-乳酸脱氢酶基因BcoaLDH和D-乳酸脱氢酶 (LdhA) 的启动子片段PldhA。将两条DNA片段连接组成了表达盒PldhA-BcoaLDH。然后将上述表达盒通过同源重组删除FMN为辅酶的L-乳酸脱氢酶编码基因lldD的同时克隆入ldhA基因缺失菌株E. coli CICIM B0013-080C (ack-pta pps pflB dld poxB adhE frdA ldhA)的染色体上,获得了L-乳酸高产菌株E. coli CICIM B0013-090B (B0013-080C,lldD::PldhA-BcoaLDH)。考察了菌株CICIM B0013-090B不同培养温度下代谢利用甘油和合成L-乳酸的特征后,建立并优化了一种新型L-乳酸变温发酵工艺。在7 L发酵罐上,发酵27 h,积累L-乳酸132.4 g/L,产酸强度4.90 g/(L·h),甘油到L-乳酸的得率为93.7％,L-乳酸的光学纯度达到99.95％。     

Succinic acid production from sucrose and molasses by metabolically engineered E. coli using a cell surface display system

To achieve sucrose-metabolizing capability, different sucrose utilization operons have been introduced into E. coli that cannot utilize sucrose. However, these engineered strains still suffer from low growth rates and low sucrose uptake rates. In this study, cell surface display system was adopted in engineered E. coli AFP111 for succinic acid production from sucrose and molasses directly. Invertase (CscA) from E. coli W was successfully anchored to outer membrane by fusion with OmpC anchoring motif, and the displayed CscA showed high extracellular activity. Compared with the sucrose permease system, the cell surface display system consumed less ATP during sucrose metabolism. When less ATP was consumed by AFP111/pTrcC-cscA, the succinic acid productivity from sucrose was 23% higher than that by AFP111/pCR2.1-cscBKA that having the sucrose permease system. As a result, 41 g L⁻¹ and 36.3 g L⁻¹ succinic acid were produced by AFP111/pTrcC-cscA from sucrose and sugarcane molasses respectively at 34 h in 3-L fermentor during dual-phase fermentation. In addition, 79 g L⁻¹ succinic acid was accumulated with recovered AFP111/pTrcC-cscA cells at the end of dual-phase fermentation in 3-L fermentor, and the overall yield was 1.19 mol mol⁻¹ hexose.     

重组大肠杆菌利用木糖发酵产高纯度L-乳酸

对重组大肠杆菌JH16利用木糖产高纯度的三一乳酸进行研究。通过无氧管驯化EscherwhiacdiJH12菌株得到E．coliJH16,驯化后的菌株茵体浓度提高了31％,乙酸积累减少了43％;在摇瓶中考察不同Mg2＋浓度对EcoliJHl6产三一乳酸的影响,确定最适Mg2＋质量浓度为0．25g/L;EcoEJH16以60g/L木糖为C源,在7L全自动发酵罐中添加0．25g／LMg2＋,乳酸积累量提高了18％,达38．18g/L,乳酸纯度高达95％;E．coliJH16在30g／L木糖和30g／L葡萄糖混合C源中,优先利用葡萄糖,当葡萄糖质量浓度低于1．56g/L后,菌体开始利用木糖进行乳酸发酵,最终得到39g／L乳酸。