Metabolic engineering of Aspergillus oryzae NRRL 3488 for increased production of l-malic acid

Malic acid, a petroleum-derived C4-dicarboxylic acid that is used in the food and beverage industries, is also produced by a number of microorganisms that follow a variety of metabolic routes. Several members of the genus Aspergillus utilize a two-step cytosolic pathway from pyruvate to malate known as the reductive tricarboxylic acid (rTCA) pathway. This simple and efficient pathway has a maximum theoretical yield of 2 mol malate/mol glucose when the starting pyruvate originates from glycolysis. Production of malic acid by Aspergillus oryzae NRRL 3488 was first improved by overexpression of a native C4-dicarboxylate transporter, leading to a greater than twofold increase in the rate of malate production. Overexpression of the native cytosolic alleles of pyruvate carboxylase and malate dehydrogenase, comprising the rTCA pathway, in conjunction with the transporter resulted in an additional 27 % increase in malate production rate. A strain overexpressing all three genes achieved a malate titer of 154 g/L in 164 h, corresponding to a production rate of 0.94 g/L/h, with an associated yield on glucose of 1.38 mol/mol (69 % of the theoretical maximum). This rate of malate production is the highest reported for any microbial system.     

酿酒酵母产苹果酸的还原TCA路径构建及发酵调控

苹果酸广泛应用于食品、化工行业。文中通过在酿酒酵母内敲除丙酮酸脱羧酶PDC1,并通过构建胞质内还原TCA的路径,即超表达丙酮酸羧化酶和苹果酸脱氢酶,成功地实现了苹果酸的生产。在野生型菌株中基本检测不到苹果酸的生成,而在工程菌株,苹果酸发酵浓度达到了45 mmol /L,同时副产物乙醇的产量也降低了18%。进一步通过发酵调控提高第二信使Ca2+的浓度使苹果酸的产量提高了7 %,在此基础上提高丙酮酸羧化酶的辅酶生物素浓度,使苹果酸的产量达到52.5 mmol /L,较原始菌株提高了16%。     

Overexpression of isocitrate lyase—glyoxylate bypass influence on metabolism in Aspergillus niger

In order to improve the production of succinate and malate by the filamentous fungus Aspergillus niger the activity of the glyoxylate bypass pathway was increased by over-expression of the isocitrate lyase (icl) gene. The hypothesis was that when isocitrate lyase was up-regulated the flux towards glyoxylate would increase, leading to excess formation of malate and succinate compared to the wild-type. However, metabolic network analysis showed that an increased icl expression did not result in an increased glyoxylate bypass flux. The analysis did show a global response with respect to gene expression, leading to an increased flux through the oxidative part of the TCA cycle. Instead of an increased production of succinate and malate, a major increase in fumarate production was observed.The effect of malonate, a competitive inhibitor of succinate dehydrogenase (SDH), on the physiological behaviour of the cells was investigated. Inhibition of SDH was expected to lead to succinate production, but this was not observed. There was an increase in citrate and oxalate production in the wild-type strain. Furthermore, in the strain with over-expression of icl the organic acid production shifted from fumarate towards malate production when malonate was added to the cultivation medium.Overall, the icl over-expression and malonate addition had a significant impact on metabolism and on organic acid production profiles. Although the expected succinate and malate formation was not observed, a distinct and interesting production of fumarate and malate was found.     

Genome-Based Metabolic Engineering of Mannheimia succiniciproducens for Succinic Acid Production

Succinic acid is a four-carbon dicarboxylic acid produced as one of the fermentation products of anaerobic metabolism. Based on the complete genome sequence of a capnophilic succinic acid-producing rumen bacterium, Mannheimia succiniciproducens, gene knockout studies were carried out to understand its anaerobic fermentative metabolism and consequently to develop a metabolically engineered strain capable of producing succinic acid without by-product formation. Among three different CO₂-fixing metabolic reactions catalyzed by phosphoenolpyruvate (PEP) carboxykinase, PEP carboxylase, and malic enzyme, PEP carboxykinase was the most important for the anaerobic growth of M. succiniciproducens and succinic acid production. Oxaloacetate formed by carboxylation of PEP was found to be converted to succinic acid by three sequential reactions catalyzed by malate dehydrogenase, fumarase, and fumarate reductase. Major metabolic pathways leading to by-product formation were successfully removed by disrupting the ldhA, pflB, pta, and ackA genes. This metabolically engineered LPK7 strain was able to produce 13.4 g/liter of succinic acid from 20 g/liter glucose with little or no formation of acetic, formic, and lactic acids, resulting in a succinic acid yield of 0.97 mol succinic acid per mol glucose. Fed-batch culture of M. succiniciproducens LPK7 with intermittent glucose feeding allowed the production of 52.4 g/liter of succinic acid, with a succinic acid yield of 1.16 mol succinic acid per mol glucose and a succinic acid productivity of 1.8 g/liter/h, which should be useful for industrial production of succinic acid.     

High yield production of four-carbon dicarboxylic acids by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Several metabolic engineered Escherichia coli strains were constructed and evaluated for four-carbon dicarboxylic acid production. Fumarase A, fumarase B and fumarase C single, double and triple mutants were constructed in a ldhA adhE mutant background overexpressing the pyruvate carboxylase from Lactococcus lactis. All the mutants produced succinate as the main four-carbon (C4) dicarboxylic acid product when glucose was used as carbon source with the exception of the fumAC and the triple fumB fumAC deletion strains, where malate was the main C4-product with a yield of 0.61–0.67 mol (mole glucose)^?1. Additionally, a mdh mutant strain and a previously engineered high-succinate-producing strain (SBS550MG-Cms pHL413-Km) were investigated for aerobic malate production from succinate. These strains produced 40.38 mM (5.41 g/L) and 50.34 mM (6.75 g/L) malate with a molar yield of 0.53 and 0.55 mol (mole succinate)^?1, respectively. Finally, by exploiting the high-succinate production capability, the strain SBS550MG-Cms243 pHL413-Km showed significant malate production in a two-stage process from glucose. This strain produced 133 mM (17.83 g/L) malate in 47 h, with a high yield of 1.3 mol (mole glucose)^?1 and productivity of 0.38 g L^?1 h^?1.     

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%。     

Enhanced production of succinic acid by metabolically engineered<Emphasis Type="Italic">Escherichia coli</Emphasis> with amplified activities of malic enzyme and fumarase

Apfl ldhA double mutantEscherichia coli strain NZN111 was used to produce succinic acid by overexpressing theE. coli malic enzyme gene (sfcA). This strain, however, produced a large amount of malic acid as well as succinic acid. After the analyses of the metabolic pathways, thefumB gene encoding the anaerobic fumarase ofE. coli was co-amplified to solve the problem of malic acid accumulation. A plasmid, pTrcMLFu, was constructed, which contains an artificial operon (sfcA-fumB) under the control of the inducibletrc promoter. From the batch culture of recombinantE. coli NZN111 harboring pTrcMLFu, 7 g/L of succinic acid was produced from 20 g/L of glucose, with no accumulation of malic acid. From the metabolic flux analysis the strain was found under reducing power limiting conditions by severe reorientation of metabolic fluxes.     

Screening,breeding and metabolic modulating of a strain producing succinic acid with corn straw hydrolyte

Purpose In this paper, the high yield mutant strain was expected to be obtained for the industrial bioconversion of corn straw hydrolyte to succinic acid. Methods API biochemical reactions and 16S r RNA sequence analysis were carried out for identification, and then the strain’s metabolic pathway and its relevant enzymes were discussed for the metabolic flux analysis (MFA). The X-ray of synchronous radiation and site-directed mutagenesis were imported for decreasing those byproducts, and the metabolic technics was also modulated. Results Identification showed that the succinic-acid-producing strain S.JST belonged to Actinobacillus succinogenes species. Metabolic pathway analysis indicated that this strain had the character of utilizing glucose and xylose simultaneously, which was a great advantage considering the fact that most crop straw hydrolyte included glucose and xylose. Metabolic flux analysis showed that acetic acid and alcohol competed with the flux of succinic acid, and the analysis of [H] reducing power balance investigated that the [H] electronic donor produced in the cell was not enough for the metabolism of succinic acid. Then X-ray mutagenesis showed that the flux of byproduct acetic acid was decreased to 0.666 from 1.233 mmol/g DW h and that two mutated sites were found in pta (gene of phosphotransacetylase) from mutant strain M.JSTP, but less succinic acid was produced due to the worse lacking in the supply of [H] reducing power. The site-directed mutagenesis showed that the flux of byproduct alcohol was successfully decreased to 0.029 from 1.303 mmol/g DW h. Then, surrounding the flux ratio of HMP to EMP, the metabolic technics was modulated with the addition of citrate in order to improve the balance of [H] reducing power, thus the succinic acid flux of the mutant M.JSTA was increased to 3.163 from 2.480 mmol/g DW h comparing with the parent strain S.JST. Conclusions The mutant strain obtained in this paper deserves to be scaled-up.     

Key Process Conditions for Production of C4 Dicarboxylic Acids in Bioreactor Batch Cultures of an Engineered Saccharomyces cerevisiae Strain

A recent effort to improve malic acid production by Saccharomyces cerevisiae by means of metabolic engineering resulted in a strain that produced up to 59 g liter⁻¹ of malate at a yield of 0.42 mol (mol glucose)⁻¹ in calcium carbonate-buffered shake flask cultures. With shake flasks, process parameters that are important for scaling up this process cannot be controlled independently. In this study, growth and product formation by the engineered strain were studied in bioreactors in order to separately analyze the effects of pH, calcium, and carbon dioxide and oxygen availability. A near-neutral pH, which in shake flasks was achieved by adding CaCO₃, was required for efficient C₄ dicarboxylic acid production. Increased calcium concentrations, a side effect of CaCO₃ dissolution, had a small positive effect on malate formation. Carbon dioxide enrichment of the sparging gas (up to 15% [vol/vol]) improved production of both malate and succinate. At higher concentrations, succinate titers further increased, reaching 0.29 mol (mol glucose)⁻¹, whereas malate formation strongly decreased. Although fully aerobic conditions could be achieved, it was found that moderate oxygen limitation benefitted malate production. In conclusion, malic acid production with the engineered S. cerevisiae strain could be successfully transferred from shake flasks to 1-liter batch bioreactors by simultaneous optimization of four process parameters (pH and concentrations of CO₂, calcium, and O₂). Under optimized conditions, a malate yield of 0.48 ± 0.01 mol (mol glucose)⁻¹ was obtained in bioreactors, a 19% increase over yields in shake flask experiments.In recent years, biologically produced 1,4-dicarboxylic acids (succinate, malate, and fumarate) have attracted great interest as more sustainable replacements for oil-derived commodity chemicals, such as maleic anhydride (50). Malate is currently mainly produced via petrochemical routes for use in food and beverages (18). Development of a biotechnological production process started in the early 1960s with the investigation of the natural malate producer Aspergillus flavus (2). Although process improvements eventually resulted in high product yields and productivities (6), the potential production of aflatoxins (20) prevented the use of this filamentous fungus in industry. Other investigated natural malate-producing fungi (listed in reference 51) produced insufficient malate for industrial use. With the rational design options of metabolic engineering, microorganisms that do not naturally produce large amounts of malic acid may also be considered as production platforms. Wild-type Saccharomyces cerevisiae strains produce little if any malate but would be an interesting starting point for the construction of an efficient malate producer. This yeast has a relatively high tolerance to organic acids and low pH, and due to its role as a model organism in research, a well-developed metabolic engineering toolbox is available. In addition, wild-type S. cerevisiae strains have GRAS (Generally Regarded As Safe) status, so that modified strains are more likely to be allowed in the production of food-grade malic acid.One of the main challenges in the development of an organic acid-producing strain of S. cerevisiae has been the elimination of ethanol formation, which in wild-type strains occurs even under aerobic conditions when glucose concentrations are high (45). Deletion of the pyruvate decarboxylase-encoding genes was found to prevent ethanolic fermentation (17). After evolutionary engineering to remove the growth defects usually associated with pyruvate decarboxylase-negative S. cerevisiae strains, a strain was obtained that produced large amounts of pyruvate, a direct precursor to malate, when grown on glucose (42). Subsequent overexpression of the anaplerotic enzyme pyruvate carboxylase, a cytosolically relocalized malate dehydrogenase and a heterologous malate transporter from Schizosaccharomyces pombe led to a strain that produced significant amounts of malate (51). Cultivation in calcium carbonate (CaCO₃)-buffered shake flasks resulted in malate titers of up to 59 g liter⁻¹ at a yield of 0.42 mol (mol glucose)⁻¹.There are many differences between cultivation in shake flasks and cultivation in (laboratory or industrial) bioreactors. As shake flask cultures lack online pH monitoring and control, there is often significant pH variation over time. The pH is of particular importance. If the yeast can be persuaded to produce organic acids at lower pH values, this reduces the need for active neutralization and thereby reduces by-product formation such as gypsum. However, thermodynamic constraints on acid export, as well as increased stress levels from (undissociated) acid and the low pH, often limit the ability of the microorganisms to produce acids at low pH (32, 43). For this reason, the poorly soluble compound CaCO₃ has traditionally been used to maintain a near-neutral pH in malic acid-producing microbial cultures (6, 29, 51). Adding CaCO₃ also gives increased concentrations of bicarbonate (and thereby CO₂), a substrate for pyruvate carboxylase in the carboxylation of pyruvate (a C₃ carbon molecule) to oxaloacetate (C₄ carbon), as well as calcium. Calcium is known to be involved in cellular signaling pathways (22, 26, 33, 46) and to influence pyruvate carboxylase activity (21, 24). Finally, oxygen transfer rates in shake flasks are often poor compared to those in stirred (laboratory) bioreactors. The formation of significant concentrations (25 g liter⁻¹) of glycerol, a well-known redox sink in S. cerevisiae (41), in shake flask cultures of the engineered malate-producing strain (51) was a strong indication of oxygen limitation.Initial experiments in aerobic, pH-controlled bioreactor cultures of the malate- and succinate-producing Saccharomyces cerevisiae strain RWB525 yielded only low concentrations of these C₄ dicarboxylic acids. The goal of the present study was to identify process parameters that explain the different production levels in shake flask and bioreactor cultures. To this end, we analyzed, both separately and in combination, the impact of culture pH and concentrations of calcium, carbon dioxide, and oxygen on the production of malate and succinate.     

Metabolic engineering of Pichia pastoris for malic acid production from methanol

The application of rational design in reallocating metabolic flux to accumulate desired chemicals is always restricted by the native regulatory network. In this study, recombinant Pichia pastoris was constructed for malic acid production from sole methanol through rational redistribution of metabolic flux. Different malic acid accumulation modules were systematically evaluated and optimized in P. pastoris. The recombinant PP‐CM301 could produce 8.55 g/L malic acid from glucose, which showed a 3.45‐fold increase compared to the parent strain. To improve the efficiency of site‐directed gene knockout, NHEJ‐related protein Ku70 was destroyed, whereas leading to the silencing of heterogenous genes. Hence, genes related to by‐product generation were deleted via a specially designed FRT/FLP system, which successfully reduced succinic acid and ethanol production. Furthermore, a key node in the methanol assimilation pathway, glucose‐6‐phosphate isomerase was knocked out to liberate metabolic fluxes trapped in the XuMP cycle, which finally enabled 2.79 g/L malic acid accumulation from sole methanol feeding with nitrogen source optimization. These results will provide guidance and reference for the metabolic engineering of P. pastoris to produce value‐added chemicals from methanol.     

Improved Succinic Acid Production in the Anaerobic Culture of an Escherichia coli pflB ldhA Double Mutant as a Result of Enhanced Anaplerotic Activities in the Preceding Aerobic Culture

Escherichia coli NZN111 is a pflB ldhA double mutant which loses its ability to ferment glucose anaerobically due to redox imbalance. In this study, two-stage culture of NZN111 was carried out for succinic acid production. It was found that when NZN111 was aerobically cultured on acetate, it regained the ability to ferment glucose with succinic acid as the major product in subsequent anaerobic culture. In two-stage culture carried out in flasks, succinic acid was produced at a level of 11.26 g/liter from 13.4 g/liter of glucose with a succinic acid yield of 1.28 mol/mol glucose and a productivity of 1.13 g/liter·h in the anaerobic stage. Analyses of key enzyme activities revealed that the activities of isocitrate lyase, malate dehydrogenase, malic enzyme, and phosphoenolpyruvate (PEP) carboxykinase were greatly enhanced while those of pyruvate kinase and PEP carboxylase were reduced in the acetate-grown cells. The two-stage culture was also performed in a 5-liter fermentor without separating the acetate-grown NZN111 cells from spent medium. The overall yield and concentration of succinic acid reached 1.13 mol/mol glucose and 28.2 g/liter, respectively, but the productivity of succinic acid in the anaerobic stage dropped to 0.7 g/liter·h due to cell autolysis and reduced anaplerotic activities. The results indicate the great potential to take advantage of cellular regulation mechanisms for improvement of succinic acid production by a metabolically engineered E. coli strain.     

Malic acid production by an electrochemical reduction system combined with the use of diaphorase and methylviologen

A regenerating reaction combined with the use of native malate dehydrogenase, native diaphorase, methylviologen, NAD, oxalacetic acid as the substrate and lipoamide as a stabilizer was carried out in the presence of electrolysis. Consequently, malic acid was efficiently produced from oxalacetic acid in the regenerating reaction. A glassy carbon bead electrode was used as a cathode. Twenty four milliamperes were passed at a rotation speed of 500 rpm, 29.8 +/- 0.3 degrees C and -1.0 V. It was found that lipoamide has a stabilizing effect on malate dehydrogenase and diaphorase. Low concentration (50 muM) of NAD was also effective for the stabilization of malate dehydrogenase. NADH regeneration activity based on malic acid production rate was 4.7 U/mg of the enzyme protein of the commercial diaphorase preparation. The current efficiency was more than 74%, compared with the theoretical yield, in the presence of enough oxalacetic acid.     

Strain variation in Hymenolepis diminuta: enzyme profiles

In comparative study of respiratory metabolism, it was established that the relative proportions of respiratory end-products (succinic, acetic and lactic acids) differed consistently in two strains of Hymenolepis diminuta (Toronto and ANU). The ANU strain produced more lactic acid and less succinic acid under aerobic and anaerobic conditions. In the shift from aerobic to anaerobic conditions both strains compensated by increasing their outputs of succinic acid. The ANU strain possessed significantly higher activities of hexokinase, pyruvate kinase, lactate dehydrogenase, cytosolic and mitochondrial malic enzyme and cytosolic α-glycerophosphate dehy drogenase. The Toronto strain had significantly higher activities of fumarase, succinate dehydrogenase, and fumarate reductase. There were no significant differences in the activities of phosphoenolpyruvate carboxykinase and malic dehydrogenase between strains. The fumarase activity in the Toronto strain was 16 times that of the ANU strain, its K_m (malate) was 0.8mM, as opposed to 2.5 mM, and it was less sensitive to inhibition by NAD or ATP. These observations are consistent with the patterns of end-product formation in the two strains. Ratios of end-products and calculations of approximate redox balance suggest that the Toronto strain may have a greater capacity for aerobic metabolism.     

Regulation of mitochondrial and cytosolic malic enzymes from cultured rat brain astrocytes

Malate has a number of key roles in the brain, including its function as a tricarboxylic acid (TCA) cycle intermediate, and as a participant in the malate-aspartate shuttle. In addition, malate is converted to pyruvate and CO₂ via malic enzyme and may participate in metabolic trafficking between astrocytes and neurons. We have previously demonstrated that malate is metabolized in at least two compartments of TCA cycle activity in astrocytes. Since malic enzyme contributes to the overall regulation of malate metabolism, we determined the activity and kinetics of the mitochondrial and cytosolic forms of this enzyme from cultured astrocytes. Malic enzyme activity measured at 37°C in the presence of 0.5 mM malate was 4.15±0.47 and 11.61±0.98 nmol/min/mg protein, in mitochondria and cytosol, respectively (mean±SEM, n=18–19). Malic enzyme activity was also measured in the presence of several endogenous compounds, which have been shown to alter intracellular malate metabolism in astrocytes, to determine if these compounds affected malic enzyme activity. Lactate inhibited cytosolic malic enzyme by a noncompetitive mechanism, but had no effect on the mitochondrial enzyme. -Ketoglutarate inhibited both cytosolic and mitochondrial malic enzymes by a partial noncompetitive mechanism. Citrate inhibited cytosolic malic enzyme competitively and inhibited mitochondrial malic enzyme noncompetitively at low concentrations of malate, but competitively at high concentrations of malate. Both glutamate and aspartate decreased the activity of mitochondrial malic enzyme, but also increased the affinity of the enzyme for malate. The results demonstrate that mitochondrial and cytosolic malic enzymes have different kinetic parameters and are regulated differently by endogenous compounds previously shown to alter malate metabolism in astrocytes. We propose that malic enzyme in brain has an important role in the complete oxidation of anaplerotic compounds for energy.These data were presented in part at the meeting of the American Society for Neurochemistry in Richmond, Virginia, March 1993     

Das Vorkommen von Malatenzym und Malo-Lactat-Enzym bei verschiedenen Milchsäurebakterien

1. Malic enzyme was induced by malic acid and malo-lactic enzyme was induced by malic acid and glucose in cells of three strains ofLactobacillus casei that were able to grow on malate as carbon source. Two strains ofStreptococcus faecalis formed malic enzyme only, whereas only malo-lactic enzyme was formed by a glucose requiring strain ofStreptococcus lactis.
2. Given sequential induction, cells ofLactobacillus casei M40 were found to contain malic enzyme and malo-lactic enzyme simultaneously.
3. Malic enzyme and malo-lactic enzyme have been separated by chromatography on Sephadex G-200. These two enzymes have a different pH optimum, different affinities for substrates, form different end products from malate, and have molecular weights of 120000 and 150000 daltons respectively.

     

A Novel Strategy Involved Anti-Oxidative Defense: The Conversion of NADH into NADPH by a Metabolic Network

The reduced nicotinamide adenine dinucleotide phosphate (NADPH) is pivotal to the cellular anti-oxidative defence strategies in most organisms. Although its production mediated by different enzyme systems has been relatively well-studied, metabolic networks dedicated to the biogenesis of NADPH have not been fully characterized. In this report, a metabolic pathway that promotes the conversion of reduced nicotinamide adenine dinucleotide (NADH), a pro-oxidant into NADPH has been uncovered in Pseudomonas fluorescens exposed to oxidative stress. Enzymes such as pyruvate carboxylase (PC), malic enzyme (ME), malate dehydrogenase (MDH), malate synthase (MS), and isocitrate lyase (ICL) that are involved in disparate metabolic modules, converged to create a metabolic network aimed at the transformation of NADH into NADPH. The downregulation of phosphoenol carboxykinase (PEPCK) and the upregulation of pyruvate kinase (PK) ensured that this metabolic cycle fixed NADH into NADPH to combat the oxidative stress triggered by the menadione insult. This is the first demonstration of a metabolic network invoked to generate NADPH from NADH, a process that may be very effective in combating oxidative stress as the increase of an anti-oxidant is coupled to the decrease of a pro-oxidant.     

Repression of sporulation in Bacillus subtilis by L-malate.

L-Malate repressed sporulation in the wild-type strain of Bacillus subtilis. When 75 mM L-malate was added to the growth medium at the time of inoculation, the appearance of heat-resistant spores was delayed 6 to 8 h. The synthesis of extracellular serine protease, alkaline phosphatase, glucose dehydrogenase, and dipicolinic acid was similarly delayed. Sporulation was not repressed when malate was added to the culture at t4 or later. A mutant was selected for ability to sporulate in the presence of malate. This strain could also sporulate in the presence of glucose. The malate-resistant mutant grew poorly with malate as sole carbon source, although it possessed an intact citric acid cycle, and it showed increased levels of malic enzyme. This indicates a defect in the metabolism of malate in the mutant. A mutant lacking malate dehydrogenase activity was also able to sporulate in the presence of malate. A model for the regulation of sporulation by malate is presented and discussed. Citric acid cycle intermediates other than malate did not affect sporulation. In contrast to previous results, sporulation of certain citric acid cycle mutants could be greatly increased or completely restored by the addition of intermediates after the enzymatic block. The results indicate that the failure of citric acid cycle mutants to sporulate can be adequately explained by lack of energy and lack of glutamate.