果糖和麦芽糖作为有氧碳源对大肠杆菌NZN111两阶段发酵中厌氧发酵的影响

为了了解磷酸转移酶转运系统 (PTS) 依赖和非PTS依赖代谢的糖类对大肠杆菌生产琥珀酸的影响,进行了两阶段培养,有氧阶段采用PTS依赖型的果糖或非PTS依赖型的麦芽糖作为丙酮酸甲酸裂解酶 (PFL) 和乳酸脱氢酶 (LDH) 双突变株NZN111的碳源,研究其对NZN111厌氧阶段代谢葡萄糖的影响。5 L罐发酵结果表明,以果糖和麦芽糖为碳源有氧培养的细胞恢复了在厌氧条件下快速代谢葡萄糖的能力,琥珀酸和丙酮酸成为主要代谢产物,最终琥珀酸得率分别为0.84和0.75 mol/mol,丙酮酸得率分别达到了0.65和0.83 mol/mol,琥珀酸和丙酮酸终浓度比分别为1.73∶1和1.21∶1。果糖和麦芽糖培养的NZN111与葡萄糖培养的菌体代谢的明显差异推测是cyclic AMP (cAMP) 依赖型和非cAMP依赖型的分解代谢物阻遏调控这两种机制共同作用的结果。     

产琥珀酸重组大肠杆菌的发酵性能研究

研究了重组大肠杆菌JM001(△ppc)/pTrc99a-pck发酵产琥珀酸的性能,结果表明厌氧条件下其耗糖能力和产酸能力分别为对照菌株JM001的4.2倍和15.3倍。进一步优化发酵条件表明：采用接入菌泥的发酵方式比按照10%接种量转接厌氧发酵的效果要好,琥珀酸的对葡萄糖的质量收率提高了约10%,且副产物乙酸的量进一步降低。初始葡萄糖浓度高于60g/L时会对菌株的生长和产酸产生抑制,且浓度越高,抑制作用越明显。7L发酵罐放大实验中,整个厌氧发酵阶段葡萄糖的消耗速率为0.42g/(L.h),琥珀酸对葡萄糖的质量收率为67.75%,琥珀酸的生产强度为0.28g/(L.h)。     

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。     

敲除frdB基因对大肠杆菌厌氧混合酸发酵的影响

以SPUEC101(产琥珀酸)为出发菌,利用RED同源重组技术敲除延胡索酸还原酶基因frdB,得到重组菌株SPUEC103(△frdB),通过减少延胡索酸生成琥珀酸的通量,实现延胡索酸的积累。实验结果表明:敲除frdB基因后,缺陷菌株生长速率降低,利用葡萄糖的能力也有所降低,同时敲除frdB基因较大程度地改变琥珀酸、延胡索酸等的分布,在两阶段发酵中,当发酵培养基中添加30 g/L的葡萄糖时,琥珀酸和延胡索酸得率最高,对比SPUEC101,SPUEC103的琥珀酸产量产率由24.6%下降为15.4%,并有延胡索酸和少量的苹果酸生成,分别为0.182±0.002 g/L和0.023±0.002 g/L,同时丙酮酸和乙酸含量也略有升高,分别由1.87±0.02 g/L、0.012±0.002 g/L上升到2.36±0.03 g/L、0.862±0.012 g/L。     

进化代谢选育高渗透压耐受型产琥珀酸大肠杆菌

在以碳酸钠为酸中和剂的大肠杆菌两阶段发酵产琥珀酸的过程中,由于Na+的积累造成发酵体系中渗透压的提高,严重抑制了琥珀酸的产物浓度。为了增强大肠杆菌对渗透压的耐受性,考察了利用进化代谢方法筛选高渗透压耐受型高产琥珀酸大肠杆菌菌株的可行性。进化代谢系统作为一种菌株突变装置,可以使菌体在连续培养条件下以最大的生长速率生长。以NaCl为渗透压调节剂,通过在连续培养装置中逐步提高NaCl浓度使菌体在高渗透压条件下快速生长,最终得到了一株高渗透压耐受型琥珀酸生产菌株Escherichia coli XB4。以碳酸钠为酸中和剂,在7 L发酵罐中利用Escherichia coli XB4进行两阶段发酵,厌氧培养60 h后,琥珀酸产量达到了69.5 g/L,琥珀酸生产速率达到了1.81 g/(L.h),分别比出发菌株提高了18.6%和20%。     

调控大肠杆菌胞内ATP和NADH水平促进琥珀酸生产

琥珀酸作为一种重要的C4平台化合物,广泛应用于食品、化学、医药等领域。利用大肠杆菌(Escherichia coli)发酵生产琥珀酸受胞内辅因子不平衡的影响,存在产率低、生产强度低、副产物多等问题。为此,对不同氧气条件下琥珀酸产量和化学计量学分析发现,微厌氧条件下E.coli FMME-N-26高效积累琥珀酸需要借助三羧酸循环(tricarboxylic acid cycle,TCA)为还原性三羧酸途径(reductive tricarboxylic acid pathway,r-TCA)提供足够的ATP和NADH。通过减少ATP消耗、强化ATP合成、阻断NADH竞争途径和构建NADH回补路径等代谢工程策略,组合调控胞内ATP与NADH含量,获得工程菌株E.coli FW-17。通过发酵条件优化,菌株E.coli FW-17在5 L发酵罐能积累139.52 g/L琥珀酸,比出发菌株提高了17.81%,乙酸浓度为1.40 g/L,降低了67.59%。进一步在1000 L发酵罐中进行放大实验,琥珀酸产量和乙酸浓度分别为140.2 g/L和1.38 g/L。     

采用玉米秸秆水解糖和玉米浆发酵生产丁二酸

研究了以玉米秸秆水解糖为碳源,不同氮源条件下琥珀酸放线杆菌Actinobacillus succinogenesSF-9的丁二酸发酵产酸能力。结果表明玉米浆可以替代酵母膏作为丁二酸发酵的廉价氮源。厌氧摇瓶丁二酸发酵单因素试验,得到在初糖浓度50 g/L时,玉米浆的较佳用量为20 g/L。在5 L搅拌罐上,考察了不同初始玉米秸秆水解糖浓度对A.succinogenes SF-9发酵生产丁二酸的影响,结果显示高初始秸秆糖浓度对琥珀酸放线杆菌的生长有抑制作用。采用补料分批发酵,发酵60 h丁二酸的产量达到42.7g/L,丁二酸产率82.7%,生产强度0.81 g/(L·h)。丁二酸的产量和生产强度较分批发酵有明显提高。     

大肠杆菌木糖生物合成琥珀酸的代谢工程研究

目的:对大肠杆菌进行代谢网络改造,考察木糖好氧发酵生产琥珀酸的可行性。方法:以有氧条件下大肠杆菌木糖生物合成琥珀酸的代谢途径分析为基础,以大肠杆菌BL21为出发菌株,通过P1噬菌体一步敲除法敲除琥珀酸脱氢酶基因(sdhA)、磷酸转乙酰基酶基因(pta)、丙酮酸脱氢酶基因(poxB)及异柠檬酸裂解酶阻遏物基因(iclR),构建木糖好氧发酵生产琥珀酸的大肠杆菌工程菌JLS400(△poxB△pta△iclR△sdhA)。将携带磷酸烯醇式丙酮酸羧化酶基因的质粒pJW225转化到JLS400中。结果:摇瓶发酵结果表明,构建的工程菌能以木糖为碳源,在好氧发酵条件下琥珀酸产率较高,副产物仅有少量乙酸和丙酮酸。结论:基因工程大肠杆菌JLS400pJW225的构建,为有氧条件下以木糖为原料生产琥珀酸的进一步研究奠定了基础。     

产L-苹果酸重组大肠杆菌的构建

基于产琥珀酸重组大肠杆菌E.coli B0013-1050的琥珀酸合成途径,利用Red同源重组技术结合Xer/dif重组系统敲除富马酸酶基因fumB、fumC,苹果酸酶基因maeB,构建L-苹果酸合成途径,最终得到重组大肠杆菌E.coli2030,该菌株在15 L发酵罐中,产L-苹果酸12.5 g/L,葡萄糖-苹果酸转化率为52.1%,同时对发酵产物中主要杂酸丙酮酸和琥珀酸的生产原因进行了初步的探讨与分析。为进一步提高L-苹果酸的转化率,整合表达来源于黄曲霉的苹果酸脱氢酶基因,构建重组菌E.coli 2040,在15 L发酵罐中产L-苹果酸14 g/L,葡萄糖-苹果酸转化率提高到60.3%。     

酶水解菊芋糖浆发酵生产琥珀酸的初步研究

用产菊粉酶的一株黑曲霉菌株进行产酶发酵条件和水解条件研究,在30℃,pH 6.0,摇床转速200 r/min,发酵时间为3 d的最适产酶条件下,酶活可以达到45.9 U/mL.以总糖含量为85.2 g/L的菊芋粉为初始底物,最适酶水解条件为温度50℃,加黑曲霉培养液的量为10%(v/v),水解12 h后,水解率达到99.6%.用此酶解液在5 L搅拌发酵罐中进行琥珀酸发酵,初始还原糖浓度53.5 g/L,36 h发酵产琥珀酸43.8 g/L,琥珀酸产率0.83 g/g,糖利用率99.0%,琥珀酸生产强度1.22 g/(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%。     

Fed-batch culture of a metabolically engineered Escherichia coli strain designed for high-level succinate production and yield under aerobic conditions

An aerobic succinate production system developed by Lin et al. (Metab Eng, in press) is capable of achieving the maximum theoretical succinate yield of 1.0 mol/mol glucose for aerobic conditions. It also exhibits high succinate productivity. This succinate production system is a mutant E. coli strain with five pathways inactivated: DeltasdhAB, Delta(ackA-pta), DeltapoxB, DeltaiclR, and DeltaptsG. The mutant strain also overexpresses Sorghum vulgare pepc. This mutant strain is designated HL27659k(pKK313). Fed-batch reactor experiments were performed for the strain HL27659k(pKK313) under aerobic conditions to determine and demonstrate its capacity for high-level succinate production. Results showed that it could produce 58.3 g/l of succinate in 59 h under complete aerobic conditions. Throughout the entire fermentation the average succinate yield was 0.94+/-0.07 mol/mol glucose, the average productivity was 1.08+/-0.06 g/l-h, and the average specific productivity was 89.77+/-3.40 mg/g-h. Strain HL27659k (pKK313) is, thus, capable of large-scale succinate production under aerobic conditions. The results also showed that the aerobic succinate production system using the designed strain HL27659k(pKK313) is more practical than conventional anaerobic succinate production systems. It has remarkable potential for industrial-scale succinate production and process optimization.     

Metabolic engineering of aerobic succinate production systems in Escherichia coli to improve process productivity and achieve the maximum theoretical succinate yield

The potential to produce succinate aerobically in Escherichia coli would offer great advantages over anaerobic fermentation in terms of faster biomass generation, carbon throughput, and product formation. Genetic manipulations were performed on two aerobic succinate production systems to increase their succinate yield and productivity. One of the aerobic succinate production systems developed earlier (Biotechnol, Bioeng., 2004, accepted) was constructed with five mutations (DeltasdhAB, Deltaicd, DeltaiclR, DeltapoxB, and Delta(ackA-pta)), which created a highly active glyoxylate cycle. In this study, a second production system was constructed with four of the five above mutations (DeltasdhAB, DeltaiclR, DeltapoxB, and Delta(ackA-pta)). This system has two routes in the aerobic central metabolism for succinate production. One is the glyoxylate cycle and the other is the oxidative branch of the TCA cycle. Inactivation of ptsG and overexpression of a mutant Sorghum pepc in these two production systems showed that the maximum theoretical succinate yield of 1.0 mol/mol glucose consumed could be achieved. Furthermore, the two-route production system with ptsG inactivation and pepc overexpression demonstrated substantially higher succinate productivity than the previous system, a level unsurpassed for aerobic succinate production. This optimized system showed remarkable potential for large-scale aerobic succinate production and process optimization.     

Genetic reconstruction of the aerobic central metabolism in Escherichia coli for the absolute aerobic production of succinate

Most reported efforts to enhance production of the industrially valuable specialty chemical succinate have been done under anaerobic conditions, where E. coli undergoes mixed-acid fermentation. These efforts have often been hampered by the limitations of NADH availability, poor cell growth, and slow production. An aerobic succinate production system was strategically designed that allows E. coli to produce and accumulate succinate efficiently and substantially as a product under absolute aerobic conditions. Mutations in the tricarboxylic acid cycle (sdhAB, icd, iclR) and acetate pathways (poxB, ackA-pta) of E. coli were created to construct the glyoxylate cycle for aerobic succinate production. Experiments in flask studies showed that 14.28 mM of succinate could be produced aerobically with a yield of 0.344 mole/mole using 55 mM glucose. In aerobic batch reactor studies, succinate production rate was faster, reaching 0.5 mole/mole in 24 h with a concentration of 22.12 mM; further cultivation showed that succinate production reached 43 mM with a yield of 0.7. There was also substantial pyruvate and TCA cycle C(6) intermediate accumulation in the mutant. The results suggest that more metabolic engineering improvements can be made to this system to make aerobic succinate production more efficient. Nevertheless, this aerobic succinate production system provides the first platform for enhancing succinate production aerobically in E. coli based on the creation of a new aerobic central metabolic network.     

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     

DctA- and Dcu-independent transport of succinate in Escherichia coli: contribution of diffusion and of alternative carriers

Quintuple mutants of Escherichia coli deficient in the C(4)-dicarboxylate carriers of aerobic and anaerobic metabolism (DctA, DcuA, DcuB, DcuC, and the DcuC homolog DcuD, or the citrate/succinate antiporter CitT) showed only poor growth on succinate (or other C(4)-dicarboxylates) under oxic conditions. At acidic pH (pH 6) the mutants regained aerobic growth on succinate, but not on fumarate. Succinate uptake by the mutants could not be saturated at physiological succinate concentrations (< or =5 mM), in contrast to the wild-type, which had a K(m) for succinate of 50 microM and a V(max) of 35 U/g dry weight at pH 6. At high substrate concentrations, the mutants showed transport activities (32 U/g dry weight) comparable to that of the wild-type. In the wild-type using DctA as the carrier, succinate uptake had a pH optimum of 6, whereas succinate uptake in the mutants was maximal at pH 5. In the mutants succinate uptake was inhibited competitively by monocarboxylic acids. Diffusion of succinate or fumarate across phospholipid membranes (liposomes) was orders of magnitude slower than the transport in the wild-type or the mutants. The data suggest that mutants deficient in DctA, DcuA, DcuB, DcuC, DcuD (or CitT) contain a carrier, possibly a monocarboxylate carrier, which is able to transport succinate, but not fumarate, at acidic pH, when succinate is present as a monoanion. Succinate uptake by this carrier was inhibited by addition of an uncoupler. Growth by fumarate respiration (requiring fumarate/succinate antiport) was also lost in the quintuple mutants, and growth was not restored at pH 6. In contrast, the efflux of succinate produced during glucose fermentation was not affected in the mutants, demonstrating that, for succinate efflux, a carrier different from, or in addition to, the known Dcu and CitT carriers is used.     

Succinate synthesis and excretion by Penicillium simplicissimum under aerobic and anaerobic conditions

Succinate is an interesting chemical for industries producing food and pharmaceutical products, surfactants, detergents and biodegradable plastics. Succinate is produced mainly by a mixed-acid fermentation process using anaerobically growing bacteria. However, succinate excretion is also widespread among fungi. In this article we report results on the intracellular concentration and the excretion of succinate by Penicillium simplicissimum under aerobic and anaerobic conditions. The intracellular concentration of succinate increased slightly with the specific growth rate and strongly if the respiratory chain was inhibited by sodium azide or anaerobic conditions (N(2)). A strong increase of succinate excretion was observed if the respiratory chain was inhibited. It is suggested that succinate synthesis under functional (sodium azide) or environmental (N(2)) anaerobic conditions occurs via the reductive part of the tricarboxylic acid cycle. Succinate is then excreted because the oxidative part of the tricarboxylic acid cycle is inactive. A possible role of succinate synthesis in the regeneration of NAD ('fumarate respiration') is discussed.     

过量表达异柠檬酸裂解酶对ldh-1谷氨酸棒状杆菌产丁二酸的影响

谷氨酸棒状杆菌SA001是缺失了乳酸脱氢酶基因 (ldhA) 的菌株。为了增加厌氧条件下经异柠檬酸到丁二酸的代谢通量,以提高丁二酸的产量。将来自大肠杆菌Escherichia coli K12的异柠檬酸裂解酶基因导入谷氨酸棒状杆菌SA001 (SA001/pXMJ19-aceA) 中。该菌经0.8 mmol/L的IPTG有氧诱导12 h后,转入厌氧发酵16 h,丁二酸的产量为10.38 g/L,丁二酸的生产强度为0.83 g/(L·h)。与出发菌株比较,异柠檬酸裂解酶的酶活提高了5.8倍,丁二酸的产量提高了48%。结果表明过量表达异柠檬酸裂解酶可以增加由乙醛酸途径流向丁二酸的代谢流。