产琥珀酸放线杆菌发酵生产琥珀酸的研究进展

近年来,因瘤胃微生物产琥珀酸放线杆菌Actinobacillus succinogenes具有高的琥珀酸产量,并能够利用多种碳源进行发酵等优点,在利用发酵法生产琥珀酸领域具有广泛的应用前景和商业化价值,因而其代谢途径和发酵工艺等基础研究成为国内外研发的热点。近年来,人们在产琥珀酸放线杆菌的代谢途径、琥珀酸发酵动力学模型、新型经济培养基以及高产菌株选育等方面的研究取得了很大进展,对研发琥珀酸发酵工艺、降低生产成本和节能减耗等具有重要的理论意义。     

响应面优化产琥珀酸放线杆菌生产丁二酸

丁二酸是一种重要的C4化合物平台,可以合成一系列重要化合物。文中对产琥珀酸放线杆菌Actinobacillus succinogenes GXAS137发酵生产丁二酸培养基成分进行优化。通过单因素和Plackett-Burman试验设计筛选出影响丁二酸发酵的重要参数,采用最陡爬坡实验逼近最大丁二酸生产区域后,利用Box-Behnken设计确定重要参数的最佳水平。筛选结果表明,影响丁二酸产量的重要参数是葡萄糖、酵母提取物和碱式碳酸镁浓度。最佳条件为(g/L)：葡萄糖70.00,酵母提取物9.20,碱式碳酸镁58.10。优化后丁二酸产量达到47.64 g/L。与初始条件 (36.89 g/L) 相比,丁二酸浓度提高了30 %。在最佳工艺条件下得到的试验结果与模型预测值很吻合,说明建立的模型是有效的。     

L-亮氨酸发酵培养基优化试验

应用Plackett-Burman设计试验从L-亮氨酸基础发酵培养基的10种成分中筛选出5种重要成分,然应用响应面分析试验确定5种重要成分的最适用量。培养基优化后摇瓶分批发酵72h产L-亮氨酸18.05g/L     

响应面法优化赖氨酸发酵培养基

运用Ｂｏｘ－Ｂｅｈｋｅｎ设计的响应面试验（Ｒｅｓｐｏｎｓｅ－ｓｕｒｆａｃｅ ｅｘｐｅｒｉｍｅｎｔ）对黄色短杆菌（Ｂｒｅｕｉｂａｃｔｅｒｉｕｍ ｆｌａｕｕｍ）ＦＢ４２进行赖氨酸发酵的培养基进行了优化。响应面法对７２小时分批发酵结果的优化分析表明：硫酸铵、豆饼水解液及玉米浆三种因素对赖氨醚发酵无明显的交互作用,在硫酸铵、豆饼水解液和玉米浆的浓度分别为５％、２％和３％时,发酵液中的产酸达到５４．０６ｇ／     

响应面法优化L-谷氨酰胺发酵培养基的研究

目的:采用响应面法对L-谷氨酰胺发酵培养基成分进行优化,以提高L-谷氨酰胺发酵产量。方法:首先利用Plackett-Burman试验设计筛选出影响L-谷氨酰胺产量的主要因素葡萄糖、玉米浆和(NH4)2SO4,在此基础上采用最陡爬坡实验逼近最大响应区域,并利用中心组合设计及响应面分析法进行回归分析。结果:通过求解回归方程得到L-谷氨酰胺发酵培养基最佳浓度为葡萄糖100 g/L、玉米浆4.5 ml/L、(NH4)2SO437.2 g/L,L-谷氨酰胺产量理论最大值达41.0 g/L。结论:经模型验证,预测值与验证试验平均值接近,在优化条件下谷氨酰胺产量提高了37.6%。     

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。     

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.     

响应面分析优化L-色氨酸清液发酵培养基

L-色氨酸是八种必需氨基酸之一,随着L-色氨酸应用市场的不断扩大,进行发酵法生产L-色氨酸的研究具有重要的现实意义。为了提高L-色氨酸产量,本文利用响应面分析法对L-色氨酸清液发酵培养基进行优化。利用优化培养基进行发酵,考察清液发酵对L-色氨酸发酵过程中生物量、L-色氨酸产量、副产物生成量的影响。结果表明:在优化条件下利用清液发酵培养基发酵,乙酸含量与原工艺相比降低了(6.75±1.26)%,L-色氨酸产量提高了(16.54±1.15)%,实验值与响应面分析预测值基本相符。     

响应面法优化叶酸高产菌发酵培养基及发酵条件

采用响应面法对叶酸产生菌产朊假丝酵母Y2.12的发酵发酵培养基及发酵条件进行优化.首先,采用Plackett-Burman方法对影响发酵各因素的效应进行评价,筛选出有显著效应的3个因素：碳源乳糖、pH值和摇床转速;并通过Box-Benhnken设计和响应面分析法对这3个主要影响因素进行分析.结果表明,优化后这3个因素的最佳值为摇床转速196r/min、pH7和碳源乳糖含量为6.25%.采用优化后的发酵培养基及发酵条件进行摇瓶发酵,叶酸的含量可达23.14±0.13mg/L,取得了很好的优化效果.     

CpG基序重组菌发酵培养基的优化

目的:为提高CpG基序重组菌的发酵水平,降低CpG重组质粒的生产成本,运用响应面法优化CpG重组菌发酵培养基。方法:利用Plackett-Burman试验筛选出影响发酵水平的3个最显著因素:糖蜜、玉米浆和工业蛋白胨。然后用响应面设计试验并优化得到最显著因素的最佳浓度,并进一步通过发酵试验验证优化后的培养基。结果:得到一组具有较高菌浓及质粒产量且价格低廉的发酵用培养基:糖蜜4.5g/L,玉米浆8.5g/L,工业蛋白胨8.5g/L,甘油10mL/L,KH2PO41.5g/L,K2HPO42.3g/L,MgSO4.7H2O 0.25g/L,在此培养条件下,OD600实测值为0.6771,理论值为0.6643,两者接近,与标准LB培养基相比,质粒产量提高了15%左右。结论:最终筛选到的培养基具有较高的性价比。     

Efficient succinic acid production from high-sugar-content beverages by Actinobacillus succinogenes

This study presents the production of succinic acid (SA) by Actinobacillus succinogenes using high-sugar-content beverages (HSCBs) as feedstock. The aim of this study was the valorization of a by-product stream from the beverage industry for the production of an important building block chemical, such as SA. Three types of commercial beverages were investigated: fruit juices (pineapple and ace), syrups (almond), and soft drinks (cola and lemon). They contained mainly glucose, fructose, and sucrose at high concentration—between 50 and 1,000 g/L. The batch fermentation tests highlighted that A. succinogenes was able to grow on HSCBs supplemented with yeast extract, but also on the unsupplemented fruit juices. Indeed, the bacteria did not grow on the unsupplemented syrup and soft drinks because of the lack of indispensable nutrients. About 30–40 g/L of SA were obtained, depending on the type of HSCB, with yield ranging between 0.75 and 1.00 g_SA/g_S. The prehydrolysis step improved the fermentation performance: SA production was improved by 6–24%, depending on the HSCB, and sugar conversion was improved of about 30–50%.     

氧化还原电位对Actinobacillus succinogenes厌氧发酵生产丁二酸的影响

为提高琥珀酸放线菌Actinobacillus succinogenes CGMCC1593厌氧发酵产丁二酸的水平。研究了以葡萄糖为C源,发酵液中不同氧化还原电位（VORP）对A．succirtogenes CGMCC1593生长和代谢产物分布的影响。结果表明：菌体生长和丁二酸积累的较佳VORP分别为-220mV和-270mV;利用代谢流分析法,比较VORP在-220mV和-270mV时发酵对数生长期（8h）和稳定期（20h）的代谢通量分布,以及发酵过程中磷酸烯醇式丙酮酸（PEP）、丙酮酸（Pyr）节点,NADH通量分配的变化,由此得出在VORP为-270mV时,NADH总通量和丁二酸方向代谢通量增幅明显。在发酵过程中,通过降低VORP至-270mV,使丁二酸的产率从70％提高到85％。     

Continuous succinic acid fermentation by Actinobacillus succinogenes

Fermentations were performed in an external recycle bioreactor using CO₂ and d-glucose at feed concentrations of 20 and 40 g L⁻¹. Severe biofilm formation prevented kinetic analysis of suspended cell (‘chemostat’) fermentation, while perlite packing enhanced the volumetric productivity by increasing the amount of immobilised cells. The highest productivity of 6.35 g L⁻¹ h⁻¹ was achieved at a dilution rate of 0.56 h⁻¹. A constant succinic acid yield of 0.69 ± 0.02 g/(g of glucose consumed) was obtained and found to be independent of the dilution rate, transient state and extent of biofilm build-up – approximately 56% of the carbon that formed phosphoenolpyruvate ended up as succinate. Byproduct analysis indicated that pyruvate oxidation proceeded solely via the formate-lyase pathway. Cell growth and corresponding biofilm formation were rapid at dilution rates higher than 0.35 h⁻¹ when the product concentrations were low (succinic acid < 10 g L⁻¹), while minimal growth was observed at succinic acid concentrations above this threshold.     

发酵法生产丁二酸的化学合成培养基的筛选

以产琥珀酸放线杆菌Actinobacillus succinogenes NJ113 为出发菌株,针对该菌株筛选出含有关键生长因子的化学合成培养基,其关键因子为谷氨酸（Glu）、蛋氨酸（Met）和生物素（VH）和烟酸（VPP）。结合原发酵培养基中的磷酸缓冲盐成分,最终得到的化学合成培养基配方（g/L）： CH3COONa 1.36,NaCl 1.0,MgCl2 0.2,CaCl2 0.2,Na2HPO4 0.31,NaH2PO4 1.6, KH2PO4 3,NH4HCO3 1.57,Glu 0.87,Met 0.11,VH 0.010,VPP 0.025。在3 L发酵罐上进行验证实验,50 g/L初始葡萄糖发酵70 h,丁二酸的质量浓度为45.2 g/L,丁二酸收率达到90.4%。与之前的半合成培养基发酵制备丁二酸相比,丁二酸的收率提高了25.2%,副产物也有很大幅度的减少。     

耐铵型产琥珀酸放线杆菌的选育及铵离子对其生长代谢的影响

经硫酸二乙酯(DES)诱变,在含61～242mmol/LNH4+梯度平板中,筛选到一株耐铵型突变株YZ25,该菌株在含121mmol/LNH4+发酵培养基中,琥珀酸产量达32.68g/L,转化率为65.4%,比出发菌提高了180.5%。进一步考察了不同形态铵盐对YZ25生长的影响,结果表明添加少量铵盐能够提高突变菌的生长速率,但当超过一定量后菌株生长受到抑制,不同铵盐对菌株的抑制程度不同,硫酸铵、碳酸氢铵、氯化铵和硝酸铵对突变株YZ25的半抑制浓度分别为:215mmol/L、265mmol/L、235mmol/L、210mmol/L。为了考察铵离子对YZ25发酵产琥珀酸的影响过程,在3.0L发酵罐以氨水作为pH的调控剂发酵,结果表明在稳定期前菌株生长基本不受铵离子抑制,生物量能够达到正常水平,但是进入稳定期后铵离子抑制作用越来越明显,导致菌株生长提前结束,耗糖不完全,产酸受阻。最后结合产琥珀酸放线杆菌Actinobacillus succinogenes代谢途径分析了铵离子对菌株抑制作用的机理。     

反相高效液相色谱在发酵制备琥珀酸中的应用

对于生物法制备琥珀酸的微生物发酵体系,利用Alltech反相Prevail C18色谱柱,以25mmol／L磷酸二氢钾（pH2.5）作为流动相,在流速1mL／min时,于210nm处紫外检测器检测,能将发酵液中琥珀酸、甲酸、乙酸和乳酸完全分离并准确定量。琥珀酸等有机酸的回收率在96％～104％之间。本方法能够快速、精确测定发酵样品中主产物琥珀酸与其它有机酸含量。     

A complete industrial system for economical succinic acid production by Actinobacillus succinogenes

An industrial fermentation system using lignocellulosic hydrolysate, waste yeast hydrolysate, and mixed alkali to achieve high-yield, economical succinic acid production by Actinobacillus succinogenes was developed. Lignocellulosic hydrolysate and waste yeast hydrolysate were used efficiently as carbon sources and nitrogen source instead of the expensive glucose and yeast extract. Moreover, as a novel method for regulating pH mixed alkalis (Mg(OH)₂ and NaOH) were first used to replace the expensive MgCO₃ for succinic acid production. Using the three aforementioned substitutions, the total fermentation cost decreased by 55.9%, and 56.4 g/L succinic acid with yield of 0.73 g/g was obtained, which are almost the same production level as fermentation with glucose, yeast extract and MgCO₃. Therefore, the cheap carbon and nitrogen sources, as well as the mixed alkaline neutralize could be efficiently used instead of expensive composition for industrial succinic acid production.     

稀酸水解玉米芯制备丁二酸

利用正交设计得到稀H2SO4水解玉米芯制备混合糖液的优化工艺:玉米芯料液比1∶5(质量体积比),物料粒径250~380μm、H2SO4用量3%(体积分数)、水解温度126℃、反应时间2.5 h。此工艺条件下的总糖收率达90%,总糖质量浓度为60 g/L,发酵抑制物糠醛含量为0.87 g/L,5-羟甲基糠醛含量为0.68 g/L。在此基础上利用活性炭吸附和Ca(OH)2中和对玉米芯混合糖液进行脱毒及脱盐处理,SO42-脱除率达96%,色素脱除率为96%,糠醛、5-羟甲基糠醛及多酚类物质脱除率均高于50%。处理后的玉米芯多组分糖液作为产琥珀酸放线杆菌(Actinobacillus succino-genes)NJ113的发酵C源,当培养基中初始总糖质量浓度为50 g/L时,丁二酸收率为61.68%,丁二酸质量浓度为30.8 g/L;初始总糖质量浓度为70 g/L时,丁二酸收率仍可达50%以上,丁二酸质量浓度为35.2 g/L。发酵实验表明,将经过脱毒脱盐处理的玉米芯多组分糖液替代葡萄糖作为C源发酵制备丁二酸具有可行性。     

Adaptive evolution improves acid tolerance and succinic acid production in Actinobacillus succinogenes

Fermentation at low pH is an efficient way to improve the competitiveness of biological succinic acid-producing process. Actinobacillus succinogenes shows good performance of succinic acid production under anaerobic conditions, but its succinic acid production capability at the low-pH is inefficient due to the poor acid resistance. Herein, a mutant A. succinogenes BC-4 with improved cell growth and succinic acid production under weak acid conditions was obtained by adaptive evolution. The specific growth rate and succinic acid production of BC-4 reached 0.13 g/L/h and 20.77 g/L, which were increased by 3.25- and 2.95- fold, respectively compared with the parent strain under anaerobic condition at pH 5.8. The activities of specific enzymes with ATP generation were significantly enhanced under weak acidic conditions, resulting in 1.28-fold increase in the maximum ATP level. Membrane fatty acid composition analysis demonstrated that the ratio of saturated to unsaturated fatty acids was decreased from 1.62 to 1.44 in mutant BC-4, leading to improved intracellular pH homeostasis. Furthermore, the change from long-chain to median-chain fatty acid might lower the permeability of H⁺ into cytoplasm for survival under acid stress. These results indicated that A. succinogenes BC-4 is a promising candidate for succinic acid production under weak acid condition.