烟酸转磷酸核糖激酶和丙酮酸羧化酶共表达对大肠杆菌BA002产丁二酸的影响

大肠杆菌BA002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NADH不能及时再生为NAD+,引起胞内辅酶NAD(H)的不平衡,最终导致厌氧条件下菌株不能利用葡萄糖生长代谢。pncB是烟酸转磷酸核糖激酶 (NAPRTase) 的编码基因,通过过量表达pncB基因能够提高NAD(H)总量与维持合适的NADH/NAD+,从而恢复了厌氧条件下重组菌E. coli BA014 (BA002/pTrc99a-pncB) 的生长和产丁二酸的性能。然而,BA014在厌氧发酵过程中有大量丙酮酸积累,为进一步提高菌株的丁二酸生产能力,减少副产物丙酮酸的生成,共表达NAPRTase和来自于乳酸乳球菌 NZ9000中丙酮酸羧化酶 (PYC) 的编码基因pyc,构建了重组菌E. coli BA016 (BA002/pTrc99a-pncB-pyc)。3 L发酵罐结果表明,BA016发酵112 h后,共消耗了35.00 g/L的葡萄糖。发酵结束时,菌体OD600为4.64,产生了25.09 g/L丁二酸。通过共表达pncB和pyc基因,使BA016的丙酮酸积累进一步降低,丁二酸产量进一步提高。     

Metabolic engineering of Escherichia coli for the production of fumaric acid

Fumaric acid is a naturally occurring organic acid that is an intermediate of the tricarboxylic acid cycle. Fungal species belonging to Rhizopus have traditionally been employed for the production of fumaric acid. In this study, Escherichia coli was metabolically engineered for the production of fumaric acid under aerobic condition. For the aerobic production of fumaric acid, the iclR gene was deleted to redirect the carbon flux through the glyoxylate shunt. In addition, the fumA, fumB, and fumC genes were also deleted to enhance fumaric acid formation. The resulting strain was able to produce 1.45 g/L of fumaric acid from 15 g/L of glucose in flask culture. Based on in silico flux response analysis, this base strain was further engineered by plasmid‐based overexpression of the native ppc gene, encoding phosphoenolpyruvate carboxylase (PPC), from the strong tac promoter, which resulted in the production of 4.09 g/L of fumaric acid. Additionally, the arcA and ptsG genes were deleted to reinforce the oxidative TCA cycle flux, and the aspA gene was deleted to block the conversion of fumaric acid into L ‐aspartic acid. Since it is desirable to avoid the use of inducer, the lacI gene was also deleted. To increase glucose uptake rate and fumaric acid productivity, the native promoter of the galP gene was replaced with the strong trc promoter. Fed‐batch culture of the final strain CWF812 allowed production of 28.2 g/L fumaric acid in 63 h with the overall yield and productivity of 0.389 g fumaric acid/g glucose and 0.448 g/L/h, respectively. This study demonstrates the possibility for the efficient production of fumaric acid by metabolically engineered E. coli. Biotechnol. Bioeng. 2013; 110: 2025–2034. © 2013 Wiley Periodicals, Inc.     

Metabolic analysis of Escherichia coli in the presence and absence of the carboxylating enzymes phosphoenolpyruvate carboxylase and pyruvate carboxylase

Fermentation patterns of Escherichia coli with and without the phosphoenolpyruvate carboxylase (PPC) and pyruvate carboxylase (PYC) enzymes were compared under anaerobic conditions with glucose as a carbon source. Time profiles of glucose and fermentation product concentrations were determined and used to calculate metabolic fluxes through central carbon pathways during exponential cell growth. The presence of the Rhizobium etli pyc gene in E. coli (JCL1242/pTrc99A-pyc) restored the succinate producing ability of E. coli ppc null mutants (JCL1242), with PYC competing favorably with both pyruvate formate lyase and lactate dehydrogenase. Succinate formation was slightly greater by JCL1242/pTrc99A-pyc than by cells which overproduced PPC (JCL1242/pPC201, ppc(+)), even though PPC activity in cell extracts of JCL1242/pPC201 (ppc(+)) was 40-fold greater than PYC activity in extracts of JCL1242/pTrc99a-pyc. Flux calculations indicate that during anaerobic metabolism the pyc(+) strain had a 34% greater specific glucose consumption rate, a 37% greater specific rate of ATP formation, and a 6% greater specific growth rate compared to the ppc(+) strain. In light of the important position of pyruvate at the juncture of NADH-generating pathways and NADH-dissimilating branches, the results show that when PPC or PYC is expressed, the metabolic network adapts by altering the flux to lactate and the molar ratio of ethanol to acetate formation.     

过表达羧化途径及失活苹果酸酶基因对大肠杆菌好氧发酵产苹果酸的影响

苹果酸是一种重要的C4二羧酸,在食品、医药、化工等领域有广泛的应用。本文主要研究羧化途径强化及苹果酸酶失活对大肠杆菌好氧发酵生产苹果酸的影响。首先在大肠杆菌E2中过表达了磷酸烯醇式丙酮酸羧化酶基因ppc,得到菌株E21,苹果酸积累量从0.57 g/L提高到3.83 g/L。随后,分别过表达来自谷氨酸棒杆菌的丙酮酸羧化酶基因pyc和来自琥珀酸放线杆菌的磷酸烯醇式丙酮酸激酶pck基因,相应的工程菌株E21(pTrcpyc)和E21(pTrc-A-pck)分别产6.04和5.01 g/L苹果酸,得率分别达到0.79和0.65 mol/mol葡萄糖。敲除E21中的苹果酸酶基因mae A和mae B,苹果酸产量也显著提高了36%,达到5.21 g/L,得率为0.62 mol/mol。然而,在过表达pyc的基础上敲除苹果酸酶基因并不能进一步提高苹果酸的产量。经过摇瓶发酵条件的初步优化,菌株E21(pTrcpyc)生产12.45 g/L苹果酸,得率为0.84 mol/mol,达到理论得率的63.2%。     

Comparison of fumaric acid production by Rhizopus oryzae using different neutralizing agents

Fumaric acid fermentation in a 10-L bubble column fermenter using different neutralizing agents [CaCO(3), Ca(OH)(2), NaHCO(3)] by Rhizopus oryzae ATCC 20344 was examined. It was found that in the fermentation using CaCO(3 )as the neutralizing agent the highest fumaric acid weight yield and volumetric productivity were obtained, 53.4% and 1.03 g/L x h(-1) respectively. In the NaHCO(3) case, the fumaric acid weight yield and volumetric productivity were 33.7% and 0.69 g/L x h(-1), respectively, much lower than the CaCO(3) case. However, the NaHCO(3) alternative has advantages of cell reuse and simple downstream processing because of the high solubility of sodium fumarate. These advantages may offset the disadvantages of using NaHCO(3) as the neutralizing agent, and the overall fumaric acid weight yield and volumetric productivity will increase.     

磷酸烯醇式丙酮酸羧化酶基因的敲除对于谷氨酸棒杆菌V1生理代谢的影响

【目的】L-缬氨酸生物合成的前体物质是丙酮酸。为了增加磷酸烯醇式丙酮酸向丙酮酸的代谢流向,优化L-缬氨酸前体物质的供应,以一株积累L-缬氨酸的谷氨酸棒杆菌V1(Corynebacterium glutamicum V1)为对象,构建磷酸烯醇式丙酮酸羧化酶(PEPC)基因敲除的重组菌株C.glutamicum V1-Δpepc,并研究pepc敲除后菌株生理特性的改变。【方法】运用交叉PCR方法得到pepc基因内部缺失的同源片段Δpepc,并构建敲除质粒pK18mobsacB-Δpepc。利用同源重组技术获得pepc基因缺陷突变株C.glutamicum V1-Δpepc。采用摇瓶发酵对C.glutamicum V1-Δpepc进行发酵特性的研究。对谷氨酸棒杆菌模式菌株C.glutamicum ATCC 13032、出发菌株C.glutamicum V1和敲除菌株C.glu-tamicum V1-Δpepc的丙酮酸激酶(Pyruvate kinase,PK)、丙酮酸脱氢酶(Pyruvate dehydro-genase,PDH)、丙酮酸羧化酶(Pyruvate carboxylase,PC)分别进行测定和分析。【结果】PCR验证以及PEPC酶活测定都表明筛选到pepc缺陷的突变菌株C.glutamicum V1-Δpepc,摇瓶发酵结果表明,突变菌株C.glutamicum V1-Δpepc不再积累L-缬氨酸而是积累L-精氨酸达到7.48 g/L。酶活测定结果表明出发菌株的PDH和PC酶活均低于模式菌株C.glu-tamicum ATCC13032和重组菌株C.glutamicum V1-Δpepc,出发菌株的PK与PEPC酶活与模式菌株没有较大的差异。【结论】研究表明,通过切断PEPC参与的三羧酸循环的回补途径,增加磷酸烯醇式丙酮酸向丙酮酸的流向使丙酮酸向TCA循环的流量增加,精氨酸的累积量提高。同时,以丙酮酸为前体的L-缬氨酸和丙氨酸的积累量降低。     

Increasing the acetyl-CoA pool in the presence of overexpressed phosphoenolpyruvate carboxylase or pyruvate carboxylase enhances succinate production in Escherichia coli

An in vivo strategy to apply the activation effect of acetyl-CoA on phosphoenolpyruvate carboxylase (PEPC) and pyruvate carboxylase (PYC) to increase succinate production in Escherichia coli was studied. This approach relies on the increased intracellular acetyl-CoA and CoA levels by overexpressing E. coli pantothenate kinase (PANK). The results showed that coexpression of PANK and PEPC, and PANK and PYC, did improve succinate production compared to the individual expression of PEPC and PYC, respectively. The intracellular acetyl-CoA and CoA levels were also measured, and each showed a significant increase when the PANK was overexpressed. Another effect observed was a decrease in lactate production. The least amount of lactate was produced when PANK and PEPC, and PANK and PYC, were coexpressed. This result showed increased competitiveness of the succinate pathway at the phosphoenolpyruvate and pyruvate nodes for the carbon flux, as a result reducing the carbon flux toward the lactate pathway. The study also demonstrates a feasible method for metabolic engineering to modulate enzyme activity in vivo through specific activators and inhibitors.     

Yarrowia lipolytica mutants devoid of pyruvate carboxylase activity show an unusual growth phenotype

We have cloned and characterized the gene PYC1, encoding the unique pyruvate carboxylase in the dimorphic yeast Yarrowia lipolytica. The protein putatively encoded by the cDNA has a length of 1,192 amino acids and shows around 70% identity with pyruvate carboxylases from other organisms. The corresponding genomic DNA possesses an intron of 269 bp located 133 bp downstream of the starting ATG. In the branch motif of the intron, the sequence CCCTAAC, not previously found at this place in spliceosomal introns of Y. lipolytica, was uncovered. Disruption of the PYC1 gene from Y. lipolytica did not abolish growth in glucose-ammonium medium, as is the case in other eukaryotic microorganisms. This unusual growth phenotype was due to an incomplete glucose repression of the function of the glyoxylate cycle, as shown by the lack of growth in that medium of double pyc1 icl1 mutants lacking both pyruvate carboxylase and isocitrate lyase activity. These mutants grew when glutamate, aspartate, or Casamino Acids were added to the glucose-ammonium medium. The cDNA from the Y. lipolytica PYC1 gene complemented the growth defect of a Saccharomyces cerevisiae pyc1 pyc2 mutant, but introduction of either the S. cerevisiae PYC1 or PYC2 gene into Y. lipolytica did not result in detectable pyruvate carboxylase activity or in growth on glucose-ammonium of a Y. lipolytica pyc1 icl1 double mutant.     

Lactic acid production by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing a <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> lactate dehydrogenase gene

This work demonstrates the first example of a fungal lactate dehydrogenase (LDH) expressed in yeast. A L(+)-LDH gene, ldhA, from the filamentous fungus Rhizopus oryzae was modified to be expressed under control of the Saccharomyces cerevisiae adh1 promoter and terminator and then placed in a 2μ-containing yeast-replicating plasmid. The resulting construct, pLdhA68X, was transformed and tested by fermentation analyses in haploid and diploid yeast containing similar genetic backgrounds. Both recombinant strains utilized 92 g glucose/l in approximately 30 h. The diploid isolate accumulated approximately 40% more lactic acid with a final concentration of 38 g lactic acid/l and a yield of 0.44 g lactic acid/g glucose. The optimal pH for lactic acid production by the diploid strain was pH 5. LDH activity in this strain remained relatively constant at 1.5 units/mg protein throughout the fermentation. The majority of carbon was still diverted to the ethanol fermentation pathway, as indicated by ethanol yields between 0.25–0.33 g/g glucose. S. cerevisiae mutants impaired in ethanol production were transformed with pLdhA68X in an attempt to increase the lactic acid yield by minimizing the conversion of pyruvate to ethanol. Mutants with diminished pyruvate decarboxylase activity and mutants with disrupted alcohol dehydrogenase activity did result in transformants with diminished ethanol production. However, the efficiency of lactic acid production also decreased. Electronic Publication     

积累L-苹果酸的米根霉突变株酶活性初探

对富马酸产生菌株—米根霉ME-F10进行诱变育种的过程中, 得到一株性能稳定的高效积累L-苹果酸的突变株ME-M15。该菌株发酵96 h平均L-苹果酸产量达16.3 g/L, 较出发菌株L-苹果酸积累量平均提高3倍, 而富马酸和乙醇的积累量大幅下降。对突变株代谢途径关键酶活研究表明, 突变株富马酸酶胞质途径同功酶和乙醇脱氢酶活力较之出发菌株酶活力明显减弱, 而丙酮酸羧化酶活力无明显差别。     

Effect of Sorghum vulgare phosphoenolpyruvate carboxylase and Lactococcus lactis pyruvate carboxylase coexpression on succinate production in mutant strains of Escherichia coli

Sorghum vulgare phosphoenolpyruvate carboxylase (PEPC) and Lactococcus lactis pyruvate carboxylase (PYC) were overexpressed in Escherichia coli concurrently to improve the production of succinate, a valuable industrial specialty chemical. This coexpression system was also applied to E. coli mutant strains strategically designed by inactivating the competing pathways of succinate formation. The highest level of succinate production was observed in E. coli strains coexpressing both PEPC and PYC when compared with E. coli strains individually overexpressing either PEPC or PYC. Lactate production was also significantly reduced with PEPC and PYC coexpression. Lactate and acetate pathways were inactivated to eliminate the competing pathways of succinate formation. Results showed that inactivation of both the lactate and acetate pathways with the coexpression of PEPC and PYC was most effective in improving succinate production. Inactivating the lactate or acetate pathway alone only caused a majority of the carbon flux to shift to other metabolites rather than succinate. Coexpression of PEPC and PYC was also applied to an E. coli mutant strain deficient in lactate dehydrogenase and pyruvate:formate lyase that accumulated a substantial amount of the intermediate metabolite pyruvate during growth. Results showed that PEPC and PYC coexpression was effective in depleting pyruvate accumulation and increasing the production of metabolites.     

Efficient succinic acid production from glucose through overexpression of pyruvate carboxylase in an Escherichia coli alcohol dehydrogenase and lactate dehydrogenase mutant

An adhE, ldhA double mutant Escherichia coli strain, SBS110MG, has been constructed to produce succinic acid in the presence of heterologous pyruvate carboxylase (PYC). The strategic design aims at diverting maximum quantities of NADH for succinate synthesis by inactivation of NADH competing pathways to increase succinate yield and productivity. Additionally an operational PFL enzyme allows formation of acetyl-CoA for biosynthesis and formate as a potential source of reducing equivalents. Furthermore, PYC diverts pyruvate toward OAA to favor succinate generation. SBS110MG harboring plasmid pHL413, which encodes the heterologous pyruvate carboxylase from Lactococcus lactis, produced 15.6 g/L (132 mM) of succinate from 18.7 g/L (104 mM) of glucose after 24 h of culture in an atmosphere of CO(2) yielding 1.3 mol of succinate per mole of glucose. This molar yield exceeded the maximum theoretical yield of succinate that can be achieved from glucose (1 mol/mol) under anaerobic conditions in terms of NADH balance. The current work further explores the importance of the presence of formate as a source of reducing equivalents in SBS110MG(pHL413). Inactivation of the native formate dehydrogenase pathway (FDH) in this strain significantly reduced succinate yield, suggesting that reducing power was lost in the form of formate. Additionally we investigated the effect of ptsG inactivation in SBS110MG(pHL413) to evaluate the possibility of a further increase in succinate yield. Elimination of the ptsG system increased the succinate yield to 1.4 mol/mol at the expense of a reduction in glucose consumption of 33%. In the presence of PYC and an efficient conversion of glucose to products, the ptsG mutation is not indispensable since PEP converted to pyruvate as a result of glucose phosphorylation by the glucose specific PTS permease EIICB(glu) can be rediverted toward OAA favoring succinate production.     

The physiological effects and metabolic alterations caused by the expression of Rhizobium etli pyruvate carboxylase in Escherichia coli

Oxaloacetate (OAA) plays an important role in the tricarboxylic acid cycle and for the biosynthesis of a variety of cellular compounds. Some microorganisms, such as Rhizobium etli and Corynebacterium glutamicum, are able to synthesize OAA during growth on glucose via either of the enzymes pyruvate carboxylase (PYC) or phosphoenolpyruvate carboxylase (PPC). Other microorganisms, including Escherichia coli, synthesize OAA during growth on glucose only via PPC because they lack PYC. In this study we have examined the effect that the R. etli PYC has on the physiology of E. coli. The expressed R. etli PYC was biotinylated by the native biotin holoenzyme synthase of E. coli and displayed kinetic properties similar to those reported for alpha4 PYC enzymes from other sources. R. etli PYC was able to restore the growth of an E. coli ppc null mutant in minimal glucose medium, and PYC expression caused increased carbon flow towards OAA in wild-type E. coli cells without affecting the glucose uptake rate or the growth rate. During aerobic glucose metabolism, expression of PYC resulted in a 56% increase in biomass yield and a 43% decrease in acetate yield. During anaerobic glucose metabolism, expression of PYC caused a 2.7-fold increase in succinate concentration, making it the major product by mass. The increase in succinate came mainly at the expense of lactate formation. However, in a mutant lacking lactate dehydrogenase activity, expression of PYC resulted in only a 1.7-fold increase in succinate concentration. The decreased enhancement of succinate formation in the /dh mutant was hypothesized to be due to accumulation of pyruvate and NADH, metabolites that affect the interconversion of the active and inactive form of the enzyme pyruvate formate-lyase.     

Simultaneous Production and Recovery of Fumaric Acid from Immobilized Rhizopus oryzae with a Rotary Biofilm Contactor and an Adsorption Column

An integrated system of simultaneous fermentation-adsorption for the production and recovery of fumaric acid from glucose by Rhizopus oryzae was investigated. The system was constructed such that growing Rhizopus mycelia were self-immobilized on the plastic discs of a rotary biofilm contactor during the nitrogen-rich growth phase. During the nongrowth, production phase, the biofilm was alternately exposed to liquid medium and air upon rotation of the discs in the horizontal fermentation vessel. The product of fermentation, fumaric acid, was removed simultaneously and continuously by a coupled adsorption column, thereby moderating inhibition, enhancing the fermentation rate, and sustaining cell viability. Another beneficial effect of the removal of fumaric acid is release of hydroxyl ions from a polyvinyl pyridine adsorbent into the circulating fermentation broth. This moderates the decrease in pH that would otherwise occur. Polyvinyl pyridine and IRA-900 gave the highest loading for this type of fermentation. This fermentation system is capable of producing fumaric acid with an average yield of 85 g/liter from 100 g of glucose per liter within 20 h under repetitive fed-batch cycles. On a weight yield basis, 91% of the theoretical maximum was obtained with a productivity of 4.25 g/liter/h. This is in contrast to stirred-tank fermentation supplemented with calcium carbonate, whose average weight yield was 65% after 72 h with a productivity of 0.9 g/liter/h. The immobilized reactor was operated repetitively for 2 weeks without loss of biological activity.     

Metabolic analysis of Corynebacterium glutamicum during lactate and succinate productions under oxygen deprivation conditions

Lactate and succinate were produced from glucose by Corynebacterium glutamicum under oxygen deprivation conditions without growth. Addition of bicarbonate to the reaction mixture led not only to a 3.6-fold increase in succinate production rate, but also to a 2.3- and 2.5-fold increase, respectively, of the rates of lactate production and glucose consumption, compared to the control. Furthermore, when small amounts of pyruvate were added to the reaction mixture, acid production rates and the glucose consumption rate were multiplied by a factor ranging from 2 to 3. These phenomena were paralleled by an increase in the NAD(+)/NADH ratio, thus corroborating the view that the efficient regeneration of NAD(+) could be triggered by the addition of either bicarbonate or pyruvate. To investigate the global metabolism of corynebacteria under oxygen deprivation conditions, we engineered several strains where the genes coding for key metabolic enzymes had been inactivated by gene disruption and replacement. A lactate dehydrogenase (LDH)-deficient mutant was not able to produce lactate, suggesting this enzyme has no other isozyme. Although a pyruvate carboxylase (pyc) mutant exhibited similar behavior to that of the wild type, phosphoenolpyruvate carboxylase (ppc) mutants were characterized by a dramatic decrease in succinate production, which was concomitant to decreased lactate production and glucose consumption rates. This set of observations corroborates the view that in coryneform bacteria under oxygen deprivation conditions the major anaplerotic reaction is driven by the ppc gene product rather than by the pyc gene product. Moreover, intracellular NADH concentrations in C. glutamicum were observed to correlate to oxygen-deprived metabolic flows.     

Enhanced citrate production through gene insertion in Aspergillus niger

The effect of inserting genes involved in the reductive branch of the tricarboxylic acid (TCA) cycle on citrate production by Aspergillus niger was evaluated. Several different genes were inserted individually and in combination, i.e. malate dehydrogenase (mdh2) from Saccharomyces cerevisiae, two truncated, cytosolic targeted, fumarases (Fum1s and FumRs) from S. cerevisiae and Rhizopus oryzae, respectively, and the cytosolic soluble fumarate reductase (Frds1) from S. cerevisiae. Overexpression of these genes in their native strain backgrounds has been reported to lead to alterations in the intracellular cytosolic dicarboxylate concentrations. It was found that all the transformant strains had enhanced yield and productivities of citrate compared with the wild-type strain. The transformants also had the ability to produce citrate in trace-manganese-contaminated medium, where the wild type was unable to produce. Overexpression of FumRs and Frds1 resulted in the best citrate-producing strain in the presence of trace manganese concentrations. This strain gave a maximum yield of 0.9g citrate per g glucose and a maximum specific productivity of 0.025g citrate per g DW per h. Overexpression of mdh2 alone resulted in an increased citrate production rate only in the initial phase of the fermentations compared with the other transformants and the wild type.     

Bioproduction of fumaric acid: an insight into microbial strain improvement strategies

Fumaric acid (FA), a metabolic intermediate, has been identified as an important carbohydrate derived platform chemical. Currently, it is commercially sourced from petrochemicals by chemical conversion. The shift to biochemical synthesis has become essential for sustainable development and for the transition to a biobased economy from a petroleum-based economy. The main limitation is that the concentrations of FA achieved during bioproduction are lower than that from a chemical process. Moreover, the high cost associated with bioproduction necessitates a higher yield to improve the feasibility of the process. To this effect, genetic modification of microorganism can be considered as an important tool to improve FA yield. This review discusses various genetic modifications strategies that have been studied in order to improve FA production. These strategies include the development of recombinant strains of Rhizopus oryzae, Escherichia coli, Saccharomyces cerevisiae, and Torulopsis glabrata as well as their mutants. The transformed strains were able to accumulate fumaric acid at a higher concentration than the corresponding wild strains but the fumaric acid titers obtained were lower than that reported with native fumaric acid producing R. oryzae strains. Moreover, one plausible adoption of gene editing tools, such as Agrobacterium-mediated transformation (AMT), CRISPR CAS-9 and RNA interference (RNAi) mediated knockout and silencing, have been proposed in order to improve fumaric acid yield. Additionally, the introduction of the glyoxylate pathway in R. oryzae to improve fumaric acid yield as well as the biosynthesis of fumarate esters have been proposed to improve the economic feasibility of the bioprocess. The adoption of some of these genetic engineering strategies may be essential to enable the development of a feasible bioproduction process.     

Development of a low pH fermentation strategy for fumaric acid production by Rhizopus oryzae

Dicarboxylic acids that are produced from renewable resources are becoming attractive building blocks for the polymers industry. In this respect, fumaric acid is very interesting. Its low aqueous solubility facilitates product recovery. To avoid excessive waste salt production during downstream processing, a low pH for fumaric acid fermentation will be beneficial. Studying the influence of pH, working volume and shaking frequency on cell cultivation helped us to identify the best conditions to obtain appropriate pellet morphologies of a wild type strain of Rhizopus oryzae. Using these pellets, the effects of pH and CO(2) addition were studied to determine the best conditions to produce fumaric acid in batch fermentations under nitrogen-limited conditions with glucose as carbon source. Decreasing either the fermentation pH below 5 or increasing the CO(2) content of the inlet air above 10% was unfavourable for the cell-specific productivity, fumaric acid yield, and fumaric acid titer. However, switching off the pH control late in the batch phase did not affect these performance parameters and allowed achieving pH of 3.6. A concentration of 20 gL(-1) of fumaric acid was obtained at pH 3.6 while the average cell mass specific productivity and fumaric acid yield were the same as at pH 5.0. Consequently, relatively modest amounts of inorganic base were required for pH control, while recovery of the acid should be relatively easy at pH 3.6.