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%.     

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.     

Substrate and product inhibition kinetics in succinic acid production by Actinobacillus succinogenes

The inhibition of substrate and products on the growth of Actinobacillus succinogenes in fermentation using glucose as the major carbon source was studied. A. succinogenes tolerated up to 143 g/L glucose and cell growth was completely inhibited with glucose concentration over 158 g/L. Significant decrease in succinic acid yield and prolonged lag phase were observed with glucose concentration above 100 g/L. Among the end-products investigated, formate was found to have the most inhibitory effect on succinic acid fermentation. The critical concentrations of acetate, ethanol, formate, pyruvate and succinate were 46, 42, 16, 74, 104 g/L, respectively. A growth kinetic model considering both substrate and product inhibition is proposed, which adequately simulates batch fermentation kinetics using both semi-defined and wheat-derived media. The model accurately describes the inhibitory kinetics caused by both externally added chemicals and the same chemicals produced during fermentation. This paper provides key insights into the improvement of succinic acid production and the modelling of inhibition kinetics.     

Continuous succinic acid production by Actinobacillus succinogenes in a biofilm reactor: Steady-state metabolic flux variation

Continuous anaerobic fermentations were performed in a novel external-recycle, biofilm reactor using d-glucose and CO₂ as carbon substrates. Succinic acid (SA) yields were found to be an increasing function of glucose consumption with the succinic acid to acetic acid ratio increasing from 2.4 g g⁻¹ at a glucose consumption of 10 g L⁻¹, to 5.7 g g⁻¹ at a glucose consumption of 50 g L⁻¹. The formic acid to acetic acid ratio decreased from an equimolar value (0.77 g g⁻¹) at a glucose consumption of 10 g L⁻¹ to a value close to zero at 50 g L⁻¹. The highest SA yield on glucose and highest SA titre obtained were 0.91 g g⁻¹ and 48.5 g L⁻¹ respectively. Metabolic flux analysis based on the established C₃ and C₄ metabolic pathways of Actinobacillus succinogenes revealed that the increase in the succinate to acetate ratio could not be attributed to the decrease in formic acid and that an additional source of NADH was present. The fraction of unaccounted NADH increased with glucose consumption, suggesting that additional reducing power is present in the medium or is provided by the activation of an alternative metabolic pathway.     

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。     

琥珀酸放线杆菌发酵培养基的优化

对琥珀酸放线杆菌(Actinobacillus succinogenes)CGMCC1593发酵产生琥珀酸培养基的主要成分,及其含量进行优化。通过单因素试验,得出发酵培养基中葡萄糖、酵母膏和玉米浆的含量对产生琥珀酸有显著影响;采用响应面法(RSM),得出多元二次回归方程拟合的三种因素与琥珀酸含量间的函数关系,并根据优化结果与实验,CGMCC1593产琥珀酸达到41.69g/L。     

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。     

Process development of succinic acid production by Escherichia coli NZN111 using acetate as an aerobic carbon source

Escherichia coli strain NZN111 could convert glucose to succinic acid efficiently in anaerobic conditions after the induction of gluconeogenic carbon sources in aerobic conditions. Acetate shows a strong effect on both yield and productivity of succinic acid. In this study, the fed-batch process of succinic acid production by NZN111 using acetate in a chemically defined medium in the aerobic stage was investigated and developed. Increasing cell density could increase succinic acid with a productivity of 3.97 g/(L h) in the first 8 h of the anaerobic phase with an overall yield of 1.42 mol/mol glucose in a 5 L fermentor. However, there was strong repression from succinic acid in the later anaerobic stage. When succinic acid exceeded 30 g/L, the glucose consumption rate began to drop sharply along with the succinic acid production rate. Supplementation with glucose from 30 to 70 g/L in the anaerobic stage showed little effect on succinic acid production. Acetic acid and pyruvic acid accumulated had no effect on succinic acid formation because of their low concentration. With acetate as the sole carbon source for aerobic cultivation in the following scale-up, 60.09 g/L of succinic acid was produced with a yield of 1.37 mol/mol in a 50 L bioreactor.     

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％。     

Succinic acid production from wheat using a biorefining strategy

The biosynthesis of succinic acid from wheat flour was investigated in a two-stage bio-process. In the first stage, wheat flour was converted into a generic microbial feedstock either by fungal fermentation alone or by combining fungal fermentation for enzyme and fungal bio-mass production with subsequent flour hydrolysis and fungal autolysis. In the second stage, the generic feedstock was converted into succinic acid by bacterial fermentation by Actinobacillus succinogenes. Direct fermentation of the generic feedstock produced by fungal fermentation alone resulted in a lower succinic acid production, probably due to the low glucose and nitrogen concentrations in the fungal broth filtrate. In the second feedstock production strategy, flour hydrolysis conducted by mixing fungal broth filtrate with wheat flour generated a glucose-rich stream, while the fungal bio-mass was subjected to autolysis for the production of a nutrient-rich stream. The possibility of replacing a commercial semi-defined medium by these two streams was investigated sequentially. A. succinogenes fermentation using only the wheat-derived feedstock resulted in a succinic acid concentration of almost 16 g l^–1 with an overall yield of 0.19 g succinic acid per g wheat flour. These results show that a wheat-based bio-refinery employing coupled fungal fermentation and subsequent flour hydrolysis and fungal autolysis can lead to a bacterial feedstock for the efficient production of succinic acid.     

Ethanol production by continuous fermentation of D-(+)-cellobiose, D-(+)-xylose and sugarcane bagasse hydrolysate using the thermoanaerobe Caloramator boliviensis

The recently isolated anaerobic bacterium Caloramator boliviensis with an optimum growth temperature of 60 °C can efficiently convert hexoses and pentoses into ethanol. When fermentations of pure sugars and a pentose-rich sugarcane bagasse hydrolysate were carried out in a packed bed reactor with immobilized cells of C. boliviensis, more than 98% of substrates were converted. Ethanol yields of 0.40-0.46 g/g of sugar were obtained when sugarcane bagasse hydrolysate was fermented. These features reveal interesting properties of C. boliviensis in producing ethanol from a renewable feedstock.     

Modeling of batch fermentation kinetics for succinic acid production by Mannheimia succiniciproducens

Kinetic models are proposed for the batch production of succinic acid from glucose by Mannheimia succiniciproducens MBEL55E. The models include terms accounting for both substrate and product inhibitions. Experimental data collected from a series of batch fermentations with different initial glucose concentrations were used to estimate parameters and also to validate the models proposed. The optimal values of the parameters were approximated by minimizing the discrepancy between the model predictions and corresponding experimental data. The growth of M. succiniciproducens could be expressed by a modified Monod model incorporating inhibitions of glucose and organic acids accumulated in the culture broth. The Luedeking–Piret model was able to describe the formation of organic acids as the fermentation proceeded, in which succinic, acetic, and formic acids followed a mixed-growth-associated pattern. However, unexpectedly, lactic acid fermentation by M. succiniciproducens was nearly nongrowth-associated. In all cases, the model simulation matched well with the experimental observations, which made it possible to elucidate the fermentation characteristics of M. succiniciproducens during efficient succinic acid production from glucose. These models thus can be employed for the development and optimization of biobased succinic acid production processes.     

Green and economical production of propionic acid by Propionibacterium freudenreichii CCTCC M207015 in plant fibrous-bed bioreactor

Propionic acid production by Propionibacterium freudenreichii from molasses and waste propionibacterium cells was studied in plant fibrous-bed bioreactor (PFB). With non-treated molasses as carbon source, 12.69 ± 0.40 g l^-1 of propionic acid was attained at 120 h in free-cell fermentation, whereas the PFB fermentation yielded 41.22 ± 2.06 g l^-1 at 120 h and faster cells growth was observed. In order to optimize the fermentation outcomes, fed-batch fermentation was performed with hydrolyzed molasses in PFB, giving 91.89 ± 4.59 g l^-1 of propionic acid at 254 h. Further studies were carried out using hydrolyzed waste propionibacterium cells as substitute nitrogen source, resulting in a propionic acid concentration of 79.81 ± 3.99 g l^-1 at 302 h. The present study suggests that the low-cost molasses and waste propionibacterium cells can be utilized for the green and economical production of propionic acid by P. freudenreichii.     

CO2 fixation for succinic acid production by engineered Escherichia coli co-expressing pyruvate carboxylase and nicotinic acid phosphoribosyltransferase

In wild-type Escherichia coli, 1 mol of CO₂ was fixated in 1 mol of succinic acid generation anaerobically. The key reaction in this sequence, catalyzed by phosphoenolpyruvate carboxylase (PPC), is carboxylation of phosphoenolpyruvate to oxaloacetate. Although inactivation of pyruvate formate-lyase and lactate dehydrogenase is found to enhance the PPC pathway for succinic acid production, it results in excessive pyruvic acid accumulation and limits regeneration of NAD⁺ from NADH formed in glycolysis. In other organisms, oxaloacetate is synthesized by carboxylation of pyruvic acid by pyruvate carboxylase (PYC) during glucose metabolism, and in E. coli, nicotinic acid phosphoribosyltransferase (NAPRTase) is a rate-limiting enzyme of the NAD(H) synthesis system. To achieve the NADH/NAD⁺ ratio decrease as well as carbon flux redistribution, co-expression of NAPRTase and PYC in a pflB, ldhA, and ppc deletion strain resulted in a significant increase in cell mass and succinic acid production under anaerobic conditions. After 72 h, 14.5 g L⁻¹ of glucose was consumed to generate 12.08 g L⁻¹ of succinic acid. Furthermore, under optimized condition of CO₂ supply, the succinic acid productivity and the CO₂ fixation rate reached 223.88 mg L⁻¹ h⁻¹ and 83.48 mg L⁻¹ h⁻¹, respectively.     

Development of an industrial medium for economical 2,3-butanediol production through co-fermentation of glucose and xylose by Klebsiella oxytoca

An industrial medium containing urea as a sole nitrogen source, low levels of corn steep liquor and mineral salts as nutrition factors to retain high 2,3-butanediol production through co-fermentation of glucose and xylose (2:1, wt/wt) by Klebsiella oxytoca was developed. Urea and corn steep liquor were identified as the most significant factors by the two-level Plackett–Burman design. Steepest ascent experiments were applied to approach the optimal region of the two factors and a central composite design was employed to determine their optimal levels. Under the optimal medium, the yield of 2,3-butanediol plus acetoin relative to glucose and xylose was up to 0.428 g/g, which was 85.6% of theoretical value. The cheap nitrogen source and nutrition factors combining the co-fermentation process using lignocellulose derived glucose and xylose as the carbon source in the developed medium would be a potential solution to improve the economics of microbial 2,3-butanediol production.     

Improving the lactic acid production of Actinobacillus succinogenes by using a novel fermentation and separation integration system

This work describes the development of a novel integrated system for lactic acid production by Actinobacillus succinogenes. Fermentation and separation were integrated with the use of a microfiltration (MF) membrane, and lactic acid was recovered by resin adsorption following MF. The fermentation broth containing residual sugar and nutrients was then recycled back into the fermenter after lactic acid adsorption. This novel approach overcame the problem of product inhibition and extended the cell growth period from 41 h to 120 h. Production of lactic acid was improved by 23% to 183.4 g L⁻¹. The overall yield and productivity for glucose were 0.97 g g⁻¹ and 1.53 g L⁻¹ h⁻¹, respectively. These experimental results indicate that the integrated system could benefit continuous production of lactic acid at high levels.     

Microbial production of N-acetylneuraminic acid by genetically engineered Escherichia coli

Previously, we described the production of N-acetylneuraminic acid (NeuAc) from N-acetylglucosamine (GlcNAc) in a system combining recombinant Escherichia coli expressing GlcNAc 2-epimerase (slr1975), E. coli expressing NeuAc synthetase (neuB), and Corynebacterium ammoniagenes. However, this system was unsuitable for large-scale production because of its complexity and low productivity. To overcome these problems, we constructed a recombinant E. coli simultaneously overexpressing slr1975 and neuB. This recombinant E. coli produced 81 mM (25 g/L) NeuAc in 22 h without the addition of C. ammoniagenes cells. For manufacturing on an industrial scale, it is preferable to use unconcentrated culture broth as the source of enzymes, and therefore, a high-density cell culture is required. An acetate-resistant mutant strain of E. coli (HN0074) was selected as the host strain because of its ability to grow to a high cell density. The NeuAc aldolase gene of E. coli HN0074 was disrupted by homologous recombination yielding E. coli N18-14, which cannot degrade NeuAc. After a 22 h reaction with 540 mM (120 g/L) GlcNAc in a 5 L jar fermenter, the culture broth of E. coli N18-14 overexpressing slr1975 and neuB contained 172 mM (53 g/L) NeuAc.     

Biological conversion of wood hydrolysate to succinic acid by Anaerobiospirillum succiniciproducens

Anaerobiospirillum succiniciproducens grew on a minimal salts medium containing wood hydrolysate (equivalent to 27 g glucose l^–1) and, when supplemented with 10 g corn steep liquor l^–1 as a complex nitrogen source, succinic acid at 24 g l^–1 was obtained (yield = 88% w/w glucose). This may therefore be an economical method to produce succinic acid.     

Oil production by oleaginous yeasts using the hydrolysate from pretreatment of wheat straw with dilute sulfuric acid

This paper explores the use of the hydrolysate from the dilute sulfuric acid pretreatment of wheat straw for microbial oil production. The resulting hydrolysate was composed of pentoses (24.3 g/L) and hexoses (4.9 g/L), along with some other degradation products, such as acetic acid, furfural, and hydroxymethylfurfural (HMF). Five oleaginous yeast strains, Cryptococcus curvatus, Rhodotorula glutinis, Rhodosporidium toruloides, Lipomyces starkeyi, and Yarrowia lipolytica, were evaluated by using this hydrolysate as substrates. The results showed that all of these strains could use the detoxified hydrolysate to produce lipids while except R. toruloides non-detoxified hydrolysate could also be used for the growth of all of the selective yeast strains. C. curvatus showed the highest lipid concentrations in medium on both the detoxified (4.2 g/L) and non-detoxified (5.8 g/L) hydrolysates. And the inhibitory effect studies on C. curvatus indicated HMF had insignificant impacts at a concentration of up to 3 g/L while furfural inhibited cell growth and lipid content by 72.0% and 62.0% at 1 g/L, respectively. Our work demonstrates that lipid production is a promising alternative to utilize hemicellulosic sugars obtained during pretreatment of lignocellulosic materials.