控制发酵过程氧化还原电位优化酿酒酵母乙醇生产

利用氧化还原电极,研究了在厌氧条件下将氧化还原电位值(ORP)控制在不同水平(-50mV、-100mV、-150mV、-230mV)对乙醇发酵过程的影响。试验结果表明,不同的ORP值水平对乙醇得率,甘油形成、有机酸分泌、生物量和菌体死亡率的影响有明显的差异。当ORP为-50mV时的生物量是ORP为-100mV时的1.26倍、ORP为-150mV时的1.86倍、ORP为-230mV时的2.59倍,甘油浓度分别是后三者的1.2倍、1.1倍、1.7倍,而乙醇浓度却分别只有后三者的0.87倍、0.49倍、0.51倍。综合考虑生物量、乙醇浓度、甘油产量、残糖的测定结果,表明将ORP控制在-150mV时对乙醇发酵极为有利。说明可以用ORP电极来精确控制厌氧发酵条件,从而为酵母细胞合理分配代谢流以实现乙醇生产最优化的宏观控制提供了一种有效的手段。     

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％。     

环境因素对琥珀酸放线杆菌Actinobacillus succinogenes CGMCC 1593发酵生产丁二酸的影响

琥珀酸放线杆菌是发酵生产有应用前景的生物基原料-丁二酸的微生物。本研究室从牛瘤胃中筛选获得一株琥珀酸放线杆菌Actinobacillus succinogenes CGMCC 1593, 分析了环境气体、pH、氧化还原电位(ORP)环境因素对琥珀酸放线杆菌A. succinogenes CGMCC 1593发酵生产丁二酸的影响。结果表明: CO2不仅提供了A. succinogenes CGMCC 1593发酵生产丁二酸的最佳气体环境, 也是发酵生产丁二酸的底物之一; MgCO3是A. succinogenes CGMCC 1593发酵过程较好的pH调节剂, 发酵过程维持pH7.1~6.2, 可满足菌体生长与产酸的要求; 发酵液初始ORP过低, 不利于菌体生长, ORP在-270 mV时对丁二酸产生有利。在菌体对数生长期结束时, 通过Na2S·9H2O降低发酵液ORP到-270 mV, 发酵48 h时可产丁二酸37 g/L, 摩尔产率达到129%。这对深入研究A. succinogenes CGMCC 1593发酵生产丁二酸具有参考价值。     

环境因素对琥珀酸放线杆菌Actinobacillus succinogenes CGMCC 1593发酵生产丁二酸的影响

琥珀酸放线杆菌是发酵生产有应用前景的生物基原料-丁二酸的微生物。本研究室从牛瘤胃中筛选获得一株琥珀酸放线杆菌Actinobacillus succinogenes CGMCC 1593, 分析了环境气体、pH、氧化还原电位(ORP)环境因素对琥珀酸放线杆菌A. succinogenes CGMCC 1593发酵生产丁二酸的影响。结果表明: CO2不仅提供了A. succinogenes CGMCC 1593发酵生产丁二酸的最佳气体环境, 也是发酵生产丁二酸的底物之一; MgCO3是A. succinogenes CGMCC 1593发酵过程较好的pH调节剂, 发酵过程维持pH7.1~6.2, 可满足菌体生长与产酸的要求; 发酵液初始ORP过低, 不利于菌体生长, ORP在-270 mV时对丁二酸产生有利。在菌体对数生长期结束时, 通过Na2S·9H2O降低发酵液ORP到-270 mV, 发酵48 h时可产丁二酸37 g/L, 摩尔产率达到129%。这对深入研究A. succinogenes CGMCC 1593发酵生产丁二酸具有参考价值。     

多种通气策略下的高浓度乙醇生产

氧气在环境胁迫强的高浓度乙醇发酵中具有重要作用.考察了自絮凝酿酒酵母在多种通气策略下的乙醇发酵及絮凝状况.使用氧化还原电位(ORP)检测发酵液中氧浓度并划分了厌氧、微氧和好氧状态.厌氧条件下的终点乙醇浓度最低(119±1.5 g/L);微氧条件下使用ORP精密控制氧气供给取得较高的乙醇浓度(131±1.8和125±1.7 g/L);在通气量0.2 vvm的好氧条件下,生物量、甘油量和乙醇损失皆最大,与最优收率相比较乙醇收率降低了12.2％.高通气量增强了细胞的絮凝能力,增大了絮凝体粒径.绘制雷达图进行综合评价,恒定通气0.05 vvm的过程在乙醇生产和絮凝各方面表现均突出.     

通气对乳酸发酵过程的影响

对拟干酪乳杆菌发酵产乳酸的过程进行研究,通过改变不同的通气量(不通气、0.1vvm、0.2 vvm、0.5 vvm)确定0.1vvm的通气量最有利于产生乳酸;再通过优化通气策略,在发酵0～15 h不通空气,15～50 h通0.1 vvm空气使得乳酸的产量比全程通0.1 vvm空气又提高了11.7%,同时乳酸产率也提高了16.2%。最后通过对胞内NAD~+、NADH、乳酸脱氢酶和NADH氧化酶活性、以及发酵过程氧化还原电位(Oxidation-reduction potential,ORP)变化进行分析,阐述了通气影响乳酸发酵过程的机理。     

利用克雷伯肺炎杆菌限制性底物发酵生产1，3-丙二醇

研究了克雷伯肺炎杆菌（Klebsiella pneumoniae）批式流加发酵生产1,3-丙二醇的发酵工艺,根据1,3-丙二醇的生产和菌体生长相关的特点,采用营养基质限制性流加的发酵工艺,通过控制氮源氯化铵以保持细胞稳定生长。结果表明：过低的氮源浓度,细胞生长受到限制,影响产物1,3-PD的合成;过高的氮源浓度,细胞比生长速率增加,但1,3-PD关于消耗甘油的得率降低,用于生长和维持代谢所消耗的甘油量增加。以0.41 g/(L·h)的氮源流加速率,残余氯化铵浓度在0.1 g/L时,转化率和生产强度最高。发酵25 h～28 h后,1,3-丙二醇最终浓度达到52.03 g/L,生产强度为2.04 g/(L·h),相对于甘油的摩尔转化率为0.66,分别比氮源限制前提高了28.0 ％、35.1 ％及29.4 ％。通过限制性流加氯化铵,控制细胞的比生长速率,使底物甘油有效转变为发酵的目标产物1,3-PD,有效实现产物1,3-PD的高生产强度以及对甘油的高转化率。     

硫酸锌(ZnSO4)对米根霉发酵产乳酸的影响

[目的]为了了解无机盐与米根霉L-乳酸代谢之间的关系,提高米根霉菌株RLC41-6发酵产L-乳酸的产率与质量,研究了ZnSO4浓度与菌株乳酸代谢和细胞内乳酸脱氢酶活性的关系.[方法]在米根霉培养基中加入不同浓度ZnSO4,经过36℃培养36 h后,应用HPLC-反相色谱法测定产物中的L-乳酸含量,并利用活性PAGE分析法测定细胞内乳酸脱氢酶的活性和组成.[结果]实验结果显示,ZnSO4对除LDH1之外的其它几条同工酶都有促进作用,尤其对LDH4,LDH5作用明显,当ZnSO4浓度大于0.02％时,LDH4,LDH5达到最大水平,同时高浓度的锌离子在体外抑制了LDH的活性.当ZnSO4浓度为0.02％时LDH酶活达到最大200 U/mL,HPLC图谱表明,此时发酵产物的只有L-乳酸,且产量达到最大137g/L,乳酸转化率为91％.[结论]Zn+会影响米根霉的乳酸代谢过程,并导致发酵过程中产物类型的变化,合适浓度的ZnSO4在米根霉代谢产乳酸的过程中,提高了乳酸脱氢酶LDH的表达,抑制丙酮酸进入苹果酸和富马酸途径,从而有利于提高葡萄糖到乳酸的代谢.     

pH对米根霉发酵厨余垃圾生产L-乳酸的影响

为了强化厨余垃圾发酵L-乳酸的产量和光学纯度,研究了pH对米根霉AS3.819发酵厨余垃圾生产乳酸及其光学特性的影响。结果表明,在中温条件下(34℃),米根霉生长的最适pH为7,最适发酵条件为8。用米根霉发酵非灭菌的厨余垃圾生产乳酸,发酵液中还原糖浓度低,且呈先升高,后下降到最低的趋势。pH调节到近中性和偏碱性(pH6、7、8)的各组还原糖浓度高于偏酸性组(pH 5和对照组)。控制pH为8时,总乳酸产生速率达1 g/(L·h),L-乳酸是主要的异构体形式,L-乳酸在总乳酸中的比例在整个发酵时间段内都保持在0.75以上,L-乳酸浓度最高达到59.8 g/L,L-乳酸光学纯度可达到0.99。控制pH为8时,可以同时获得高的乳酸产量和光学纯度。     

氮源种类及溶氧水平对锁掷酵母产类胡萝卜素组分的影响

在锁掷酵母（Sporidioboluspararoseus）发酵产类胡萝卜紊的过程中,发酵产物中类胡萝卜紊种类繁多,而且性质相似,加大了不同色素分离纯化的难度。为定向积累不同种类的类胡萝卜素,以本实验室保藏锁挪酵母JD-2为出发菌,研究了氮源种类和浓度及溶氧对锁掷酵母产类胡萝卜素的影响,并在7L发酵罐中进行了补料分批发酵试验。发现培养基中同时添加有机氮源和无机氮源且溶氧控制较低（5％）时有利于β-胡萝卜素的大量积累,最佳有机氮源和无机氮源分别为玉米浆（20g／L）、硫酸铵（5g／L）。补料分批发酵时β-胡萝卜素产量达到31．28mg／L,红酵母烯12．38mg／L。培养基中只添加有机氮源且相对溶氧控制相对较高（30％）时有利于红酵母烯的大量积累,最佳有机氮源为酵母膏（20g／L）。补料分批发酵时红酵母烯产量达到38．96mg／L,8．胡萝卜素12．36mg／L。     

Effects of redox potential control on succinic acid production by engineered Escherichia coli under anaerobic conditions

The effects of oxido-reduction potential (ORP) control on succinic acid production have been investigated in Escherichia coli LL016. In LL016, two CO₂ fixation pathways were achieved and NAD⁺ supply was enhanced by co-expression of heterologous pyruvate carboxylase (PYC) and nicotinic acid phosphoribosyltransferase (NAPRTase). During anaerobic fermentation, cell growth and metabolite distribution were changed with redox potential levels in the range of −200 to −400 mV. From the results, the ORP level of −400 mV was preferable, which resulted in the high succinic acid concentration (28.6 g/L) and high succinic acid productivity (0.33 g/L/h). Meanwhile, the yield of succinic acid at the ORP level of −400 mV was 39% higher than that at the ORP level of −200 mV. In addition, a higher NADH/NAD⁺ ratio and increased enzyme activities were also achieved by regulating the culture to a more reductive environment, which further enhanced the succinic acid production.     

高糖和氮源对鼠李糖乳杆菌(Lactobacillus rhamnosus)L-乳酸发酵的影响

鼠李糖乳杆菌经实验室耐高糖高酸选育,能够在高糖浓度下高效高产L-乳酸。以酵母粉为氮源和生长因子,葡萄糖初始浓度分别为120 g/L和146 g/L,摇瓶培养120h,L-乳酸产量分别为104g/L和117.5g/L,L-乳酸得率分别为86.7%和80.5%。高葡萄糖浓度对菌的生长和乳酸发酵有一定的抑制。增加接种量,在高糖浓度发酵条件下,可以缩短发酵时间,但对增加乳酸产量效果不明显。乳酸浓度对鼠李糖乳杆菌生长和产酸有显著的影响。初始乳酸浓度到达70g/L以上时,鼠李糖乳杆菌基本不生长和产酸,葡萄糖消耗也被抑制。酵母粉是鼠李糖乳杆菌的优良氮源,使用其它被测试的氮源菌体生长和产酸都有一定程度的下降。用廉价的黄豆粉并补充微量维生素液,替代培养基中的酵母粉,可以使产酸浓度和碳源得率得以基本维持。     

An oxidoreduction potential shift control strategy for high purity propionic acid production by Propionibacterium freudenreichii CCTCC M207015 with glycerol as sole carbon source

The effects of oxidoreduction potential (ORP) regulation on the process of propionic acid production by Propionibacterium freudenreichii CCTCC M207015 have been investigated. Potassium ferricyanide and sodium borohydride were determined as ORP control agents through serum bottle experiment. In batch fermentation, cell growth, propionic acid and by-products distribution were changed with ORP levels in the range of 0–160 mV. Based on these analysis results, an ORP-shift control strategy was proposed: at first 156 h, ORP was controlled at 120 mV to obtain higher cell growth rate and propionic acid formation rate, and then it was shifted to 80 mV after 156 h to maintain the higher propionic acid formation rate. By applying this strategy, the optimal parameters were obtained as follows: the propionic acid concentration 45.99 g L^?1, productivity 0.192 g L^?1 h^?1, the proportion of propionic acid to total organic acids 92.26 % (w/w) and glycerol conversion efficiency 76.65 %. The mechanism of ORP regulation was discussed by the ratio of NADH/NAD⁺, ATP levels, and metabolic flux analysis. The results suggest that it is possible to redistribute energy and metabolic fluxes by the ORP-shift control strategy, and the strategy could provide a simple and efficient tool to realize high purity propionic acid production with glycerol as carbon source.     

Optimisation of media and cultivation conditions for L(+)(S)-lactic acid production by Lactobacillus casei NRRL B-441

Process variables and concentration of carbon in media were optimised for lactic acid production by Lactobacillus casei NRRL B-441. Lactic acid yield was inversely proportional to initial glucose concentration within the experimental area (80-160 g l(-1)). The highest lactic acid concentration in batch fermentation, 118.6 g l(-1), was obtained with 160 g 1(-1) glucose. The maximum volumetric productivity, 4.4 g 1(-1) h(-1) at 15 h, was achieved at an initial glucose concentration of 100 g l(-1). Similar lactic acid concentrations were reached with a fedbatch approach using growing cells, in which case the fermentation time was much shorter. Statistical experimental design and response surface methodology were used for optimising the process variables. The temperature and pH optima for lactic acid production were 35 degrees C, pH 6.3. Malt sprout extract supplemented with yeast extract (4 g l(-1)) appeared to be an economical alternative to yeast extract alone (22 g l(-1)) although the fermentation time was a little longer. The results demonstrated both the separation of the growth and lactic acid production phases and lactic acid production by non-growing cells without any nutrient supplements. Resting L. casei cells converted 120 g l(-1) glucose to lactic acid with 100% yield and a maximum volumetric productivity of 3.5 g l(-1) h(-1).     

菊糖芽孢乳杆菌DS2-18中试规模的D-乳酸发酵研究

研究了菊糖芽孢乳杆茵DS2的突变株DS2-18在中试规模的D-乳酸发酵.在容积为300L自控发酵罐中,DS2-18茵在合适的发酵条件下,即培养基组成(g/L):葡萄糖120,玉米浆8,蛋白胨6,豆粕水解液100,接种量8%(v/v),发酵温度40℃,以轻质碳酸钙作为中和剂调pH 5～6,发酵期间交替不通气和通气,发酵6...     

High-rate continuous production of lactic acid by Lactobacillus rhamnosus in a two-stage membrane cell-recycle bioreactor

It is important to produce L(+)-lactic acid at the lowest cost possible for lactic acid to become a candidate monomer material for promising biodegradable polylactic acid. In an effort to develop a high-rate bioreactor that provides high productivity along with a high concentration of lactic acid, the performance of membrane cell-recycle bioreactor (MCRB) was investigated via experimental studies and simulation optimization. Due to greatly increased cell density, high lactic acid productivity, 21.6 g L(-1) h(-1), was obtained in the reactor. The lactic acid concentration, however, could not be increased higher than 83 g/L. When an additional continuous stirred tank reactor (CSTR) was attached next to the MCRB a higher lactic acid concentration of 87 g/L was produced at significant productivity expense. When the two MCRBs were connected in series, 92 g/L lactic acid could be produced with a productivity of 57 g L(-1) h(-1), the highest productivity among the reports of L(+)-lactic acid that obtained lactic acid concentration higher than 85 g/L using glucose substrate. Additionally, the investigation of lactic acid fermentation kinetics resulted in a successful model that represents the characteristics of lactic acid fermentation by Lactobacillus rhamnosus. The model was found to be applicable to most of the existing data with MCRBs and was in good agreement with Levenspiel's product-inhibition model, and the Luedeking-Piret equation for product-formation kinetics appeared to be effective in representing the fermentation kinetics. There was a distinctive difference in the production potential of cells (cell-density-related parameter in Luedeking-Piret equation) as lactic acid concentration increases over 55 g/L, and this finding led to a more precise estimation of bioreactor performance.     

Strain improvement and metabolic flux analysis in the wild-type and a mutant Lactobacillus lactis strain for L(+)-lactic acid production

The effects of initial glucose concentration and calcium lactate concentration on the lactic acid production by the parent strain, Lactobacillus lactis BME5-18, were studied. The results of the experiments indicated that glucose and lactate repressed the cell growth and the lactic acid production by Lactobacillus lactis BME5-18. A L(+)-lactic acid overproducing strain, Lactobacillus lactis BME5-18M, was screened by mutagenizing the parent strain with ultraviolet (UV) light irradiation and selecting the high glucose and lactate calcium concentration repression resistant mutant. Starting with a concentration of 100g L(-1) glucose, the mutant produced 98.6 g L(-1) lactic acid after 60 h in flasks, 73.9% higher than that of the parent strain. The L(+)-lactic acid purity was 98.1% by weight based on the amount of total lactic acid. The culture of the parent strain could not be analyzed well by conventional metabolic flux analysis techniques, since some pyruvate were accumulated intracellularly. Therefore, a revised flux analysis method was proposed by introducing intracellular pyruvate pool. Further studies demonstrate that there is a high level of NADH oxidase activity (12.11 mmol mg(-1) min(-1)) in the parent strain. The molecular mechanisms of the strain improvement were proposed, i.e., the high level of NADH oxidase activity was eliminated and the uptake rate of glucose was increased from 82.1 C-mmol (g DW h)(-1) to 98.9 C-mmol (g DW h)(-1) by mutagenizing the parent strain with UV, and therefore the mutant strain converts mostly pyruvate to lactic acid with a higher productivity (1.76 g L(-1) h(-1)) than the parent strain (0.95 g L(-1) h(-1)).     

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.     

产酸丙酸杆菌生长特性及5L罐发酵动力学研究

论文在摇瓶水平对产酸丙酸杆菌基本生长特性（温度、pH、摇床转速、接种量、种龄等）、碳源、氮源利用情况、产物抑制及5 L罐发酵动力学进行了研究。结果表明,该菌在32℃,初始pH 6．5,摇床转速150 r/min,接种24 h的种子液,接种量为5％条件下,产酸丙酸杆菌生长及产酸水平达最高值;该菌可利用碳源十分广泛,但对氮源要求比较高,只可利用有机氮源;在不同初始葡萄糖浓度下,产酸丙酸杆菌生长及产酸水平差异不大,无明显底物抑制现象;在2g/L的初始丙酸盐浓度下,该菌生长受到明显抑制;在5L发酵罐中,初始葡萄糖浓度为58．8 g/L,发酵72 h,葡萄糖消耗完全,丙酸终浓度达22．4 g/L,丙酸得率和产率分别达0．381 g/g和0．295 g/（L·h）,丙酸占总酸比例达72．10％。