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)。     

发酵产丁二酸过程中废弃细胞的循环利用

对厌氧发酵产丁二酸后的废弃细胞进行破壁处理,考察了以细胞水解液作为有机氮源重新用于丁二酸发酵的可行性。比较了超声破碎、盐溶、酶解3种方法破碎细胞获得的水解液作为氮源发酵产丁二酸的效果,结果表明酶解制得的细胞水解液效果最佳。以总氮含量为1.11g/L的酶解液(相当于10g/L酵母膏)作为氮源发酵,丁二酸产量可达42.0g/L,继续增大酶解液用量对耗糖、产酸能力没有显著提高。将细胞酶解液与5g/L酵母膏联用发酵36h后,丁二酸产量达75.5g/L,且丁二酸生产强度为2.10g/(L·h),比使用10g/L酵母膏时提高了66.7%。因此,厌氧发酵产丁二酸结束后的废弃细胞酶解液可以替代原培养基中50%的酵母膏用于发酵。     

大肠杆菌AFP111利用玉米粉全水解液厌氧发酵合成丁二酸

利用双酶法制得的玉米粉糖液及制糖过程中玉米糖渣酶解后含氮水解液作为发酵培养基,考察在不添加其他营养物质条件下大肠杆菌(E.coli)AFP111专一厌氧发酵产丁二酸的可能性。结果表明:E.coli AFP111厌氧发酵48 h后,丁二酸质量浓度达到15.24 g/L,丁二酸的得率为0.76 g/g。与在LB培养基中发酵相比,产量提高了14.41%。对关键酶酶活和辅因子NAD(H)含量的测定结果显示,能利用玉米粉全水解液的苹果酸脱氢酶(MDH)、磷酸烯醇式丙酮酸(PEP)羧化酶(PPC)、PEP羧化激酶(PCK)酶活及辅因子NAD(H)含量分别为0.88 U、0.29 U、0.31 U和15.09μmol/g,均比LB培养基中关键酶酶活和辅因子NAD(H)含量高。由此推测,玉米粉全水解液中关键生长因子(D-生物素、VB1和烟酸)的含量影响了关键酶酶活和辅因子NAD(H)的含量,从而影响丁二酸的产量。在5 L罐中厌氧发酵120 h,利用玉米粉全水解液,丁二酸的得率为0.84 g/g,比利用LB培养基发酵得到的丁二酸得率提高了21.74%。     

重组大肠杆菌利用蔗糖及糖蜜发酵生产丁二酸

富含蔗糖的甘蔗糖蜜可作为制备丁二酸的廉价原料。然而生产丁二酸的潜力菌株大肠杆菌Escherichia coli AFP111不能代谢蔗糖。为了使其具有蔗糖代谢能力,将E.coli W中非PTS蔗糖利用系统蔗糖通透酶的编码基因csc B,果糖激酶的编码基因csc K和蔗糖水解酶的编码基因csc A克隆并表达到AFP111中,获得重组菌株AFP111/p MD19T-csc BKA。经厌氧发酵验证,重组菌株72 h消耗20 g/L蔗糖,丁二酸产量达到12 g/L。在3L发酵罐中采用有氧阶段培养菌体、厌氧阶段发酵的两阶段发酵方式,厌氧发酵30 h,重组菌株以蔗糖和糖蜜为碳源丁二酸产量分别为34 g/L和30 g/L。结果表明,通过外源引入非PTS蔗糖利用系统,重组菌株具有较强的代谢蔗糖生长及合成丁二酸的能力,并且能够利用廉价糖蜜发酵制备丁二酸。     

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%。     

里氏木霉306产t-PA固态发酵条件的研究

对基因工程菌株里氏木霉(Trichodermareesei)306生物合成组织型纤溶酶原激活剂(t-PA)的固态发酵培养基成分和发酵条件进行了研究;分析了发酵过程中t-PA的生成、总糖的消耗和菌体生长的规律。在优化的固体发酵条件下,t-PA的最大酶活是924.63IU/g干重培养基,较初始条件下提高了5倍。通过浅盘进行了放大实验,最大酶活为983.64IU/g干重培养基,t-PA合成速率为:13.66IU/g干重培养基.h,较三角瓶固态发酵最高产酶提高了6.38%,产酶速率提高了24.07%。     

进化代谢选育高浓度NH_4~+耐受型产丁二酸大肠杆菌

利用大肠杆菌厌氧制备丁二酸过程中,采用氨水作为p H调节剂不仅可以中和酸性产物还可提供无机氮,被菌体利用,然而高浓度NH_4~+的积累会抑制菌体生长及代谢产酸的能力。为增强大肠杆菌对高浓度NH_4~+的耐受性,以(NH4)2HPO4为NH_4~+供体,通过在连续培养装置中不断提高(NH_4)_2HPO4浓度,以获得可耐受0.53 mol/L NH_4~+的产丁二酸大肠杆菌。结果表明:突变株在0.53 mol/L NH_4~+胁迫下,摇瓶厌氧发酵72 h,细胞干质量浓度(DCW)可达1.82 g/L,丁二酸产量为11.72 g/L,分别比出发菌株提高了1.6和4.6倍。进一步地,在5 L发酵罐上考察其利用氨水调节p H生产丁二酸的能力,厌氧发酵90 h,丁二酸质量浓度达到27.32 g/L,生产强度为0.30g/(L·h),比出发菌株分别提高88.1%和87.5%。     

产丁二酸工程菌的构建及其厌氧发酵

为了考察过量表达苹果酸酶对于E.coli NZN111(ldhA::Kan pfl::Cam)厌氧发酵产丁二酸的影响, 将连接有苹果酸酶基因sfcA的表达载体pTrc99a-sfcA转化进NZN111中, 构建了重组NZN111(pTrc99a-sfcA)。0.5 mmol/L IPTG诱导8 h后, 测定的苹果酸酶比酶活为30.67 u/mg, 比受体菌提高了140倍。采用两阶段发酵模式, 结果表明: 过量表达的苹果酸酶在NZN111体内催化了从丙酮酸到苹果酸的逆向反应, 丁二酸是发酵过程中积累的主要有机酸, 且当加入0.7 mmol/L IPTG诱导, 初始葡萄糖糖浓度为18.5 g/L时, 选择对数生长期后期的菌种以10%的接种量转入厌氧发酵, 发酵结束时发酵液中丁二酸的浓度为12.84 g/L, 对葡萄糖的收率为69.43%, 乙酸为0.58 g/L, 二者浓度比为22:1, 没有检测到甲酸和乳酸。构建的菌种具有高产丁二酸和副产物极少的优点, 在同类菌种中处于先进水平。     

谷氨酸棒状杆菌厌氧产丁二酸的发酵条件

考察谷氨酸棒状杆菌ATCC13032Δldh厌氧产丁二酸的发酵条件。结果发现:补加NaHCO3的效果最好,并且考察了NaHCO3浓度对葡萄糖转化速率及丁二酸生成速率的影响。运用代谢流分析方法分析了乳酸脱氢酶基因敲除对谷氨酸棒状杆菌厌氧代谢的影响,发现乳酸脱氢酶基因敲除导致磷酸烯醇式丙酮酸生成丁二酸的流量提高了214.3%,流向乳酸的流量变为0;分批厌氧转化36 h生成41.2 g/L丁二酸,产率45.0%。     

GABAA受体蛋白片段在大肠杆菌细胞表达条件研究

为了提高GABAA受体α1蛋白片段在大肠杆菌中表达量,研究了重组菌的发酵条件,包括培养基,接种量,温度,摇床转速,pH,诱导培养时间和诱导剂IPTG使用浓度等对GABAA受体蛋白片段表达的影响。结果表明重组菌以LB培养基为发酵基质,按3%接种量,37℃培养细胞3.5h后IPTG32℃诱导5h,菌体生物量为3.25g/L,目标蛋白表达量达95mg/L。用16L发酵罐进行放大培养,菌体生物量达4.95g/L,发酵周期5.5h。最高目标蛋白表达量达到136mg/L。     

Production of succinic acid and lactic acid by Corynebacterium crenatum under anaerobic conditions

A new succinic acid and lactic acid production bioprocess by Corynebacterium crenatum was investigated in mineral medium under anaerobic conditions. Corynebacterium crenatum cells with sustained acid production ability and high acid volumetric productivity harvested from the glutamic acid fermentation broth were used to produce succinic acid and lactic acid. Compared with the first cycle, succinic acid production in the third cycle increased 120% and reached 43.4 g/L in 10 h during cell-recycling repeated fermentations. The volumetric productivities of succinic acid and lactic acid could maintain above 4.2 g/(L·h) and 3.1 g/(L·h), respectively, for at least 100 h. Moreover, wheat bran hydrolysates could be used for succinic acid and lactic acid production by the recycled C. crenatum cells. The final succinic acid concentration reached 43.6 g/L with a volumetric productivity of 4.36 g/(L·h); at the same time, 32 g/L lactic acid was produced.     

Maintaining high anaerobic succinic acid productivity by product removal

During dual-phase fermentations using Escherichia coli engineered for succinic acid production, the productivity and viable cell concentration decrease as the concentration of succinic acid increases. The effects of succinic acid on the fermentation kinetics, yield, and cell viability were investigated by resuspending cells in fresh media after selected fermentation times. The cellular succinic acid productivity could be restored, but cell viability continuously decreased throughout the fermentations by up to 80% and subsequently the volumetric productivity was reduced. Omitting complex nutrients in the resuspension media had no significant effect on cellular succinate productivity and yield, although the viable cell concentration and thus the volumetric productivity was reduced by approximately 20%. By resuspending the cells, the amount of succinate produced during a 100-h fermentation was increased by more than 60%. The results demonstrate that by product removal succinic acid productivity can be maintained at high levels for extended periods of time.     

Succinic acid production with metabolically engineered <Emphasis Type="Italic">E. coli</Emphasis> recovered from two-stage fermentation

Escherichia coli AFP111 cells recovered from spent two-stage fermentation broth were investigated for additional production of succinic acid under anaerobic conditions. Recovered cells produced succinic acid in an aqueous environment with no nutrient supplementation except for glucose and MgCO₃. In addition, initial glucose concentration and cell density had a significant influence on succinic acid mass yield and productivity. Although the final concentration of succinic acid from recovered cells was lower than from two-stage fermentation, an average succinic acid mass yield of 0.85 g/g was achieved with an average productivity of 1.81 g/l h after three rounds of recycling, which was comparable to two-stage fermentation. These results suggested that recovered cells might be reused for the efficient production of succinic acid.     

Economical succinic acid production from cane molasses by Actinobacillus succinogenes

In this work, production of succinic acid by Actinobacillus succinogenes CGMCC1593 using cane molasses as a low cost carbon source was developed. In anaerobic bottles fermentation, succinic acid concentration of 50.6+/-0.9 g l(-1) was attained at 60 h using an optimum medium containing molasses pretreated with sulfuric acid, resulting in a succinic acid yield of 79.5+/-1.1% and sugar utilization of 97.1+/-0.6%. When batch fermentation was carried out in a 5-l stirred bioreactor with pretreated molasses, 46.4 g l(-1) of succinic acid was attained at 48 h and faster cells growth was also observed. Fed batch fermentation was performed to minimize the substrate (sugar) inhibition effect, giving 55.2 g l(-1) of succinic acid and 1.15 g l(-1)h(-1) of productivity at 48 h. The present study suggests that the inexpensive cane molasses could be utilized for the economical and efficient production of succinic acid by A. succinogenes.     

Succinate production in dual-phase Escherichia coli fermentations depends on the time of transition from aerobic to anaerobic conditions

We examined succinic acid production in Escherichia coli AFP111 using dual-phase fermentations, which comprise an initial aerobic growth phase followed by an anaerobic production phase. AFP111 has mutations in the pfl, ldhA, and ptsG genes, and we additionally transformed this strain with the pyc gene (AFP111/pTrc99A-pyc) to provide metabolic flexibility at the pyruvate node. Aerobic fermentations with these two strains were completed to catalog physiological states during aerobic growth that might influence succinate generation in the anaerobic phase. Activities of six key enzymes were also determined for these aerobic fermentations. From these results, six transition times based on physiological states were selected for studying dual-phase fermentations. The final succinate yield and productivity depend greatly on the physiological state of the cells at the time of transition. Using the best transition time, fermentations achieved a final succinic acid concentration of 99.2 g/l with an overall yield of 110% and productivity of 1.3 g/l h. Journal of Industrial Microbiology & Biotechnology (2002) 28, 325–332 DOI: 10.1038/sj/jim/7000250 Received 01 October 2001/ Accepted in revised form 12 March 2002     

基因组改组技术选育耐酸性琥珀酸放线杆菌

以琥珀酸产生菌Actinobacillus succinogenes CGMCC 1593为出发菌,分别经过紫外线-甲基磺酸乙酯(UV-EMS)和紫外线-硫酸二乙酯(UV-DES)诱变处理,得到7株耐酸性有所提高的突变株.以此作为候选菌库,经3轮原生质体递进融合,筛选获得4株可以在pH 5.6下生长的改组菌株.其中改组菌株F3-21在pH 5.6的完全液体培养基中生长的OD值是原始菌的7倍,在pH 5.2条件下仍能生长;其摇瓶发酵48h琥珀酸产量较原始菌株提高48%.在5L发酵罐中进行分批发酵,当控制pH在较低值(5.6～6.0)时,F3-21厌氧发酵48h积累琥珀酸38.1g/L,较出发菌株提高了45%;当控制pH在6.5～7.0时,F3-21厌氧发酵32h积累琥珀酸40.7g/L.F3-21在5L发酵罐中进行补料分批发酵,厌氧发酵72h,产琥珀酸达67.4g/L.结果说明基因组改组技术能够改进琥珀酸放线菌的耐酸性能及其琥珀酸的产量.     

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     

利用嗜盐菌Salinivibrio YS生产2,3-丁二醇和琥珀酸

以从新疆艾丁湖采集的土样中分离出的中度嗜盐菌Salinivibrio YS为研究对象,利用该菌在厌氧条件下生产2,3-丁二醇和琥珀酸,在单因素摇瓶实验基础上,确定影响产物积累的各因素及其相应条件,再利用正交试验确定这些参数的最佳水平,即温度33℃,起始pH为8.0,发酵过程pH为7.0,乙酸添加量为3 g/L,NaCl浓度为l0 g/L.利用优化条件进行3L体系的发酵放大实验,经过108 h的无氧发酵,2,3-丁二醇的产量可达35.05 g/L,而琥珀酸的含量则高达22.46 g/L,且其糖的总转化率高达约50％.首次利用嗜盐菌在厌氧条件下生产2,3-丁二醇和琥珀酸,拓展了嗜盐菌的应用,同时也为生产2,3-丁二醇和琥珀酸提供了新的思路.