The Separative Bioreactor: A Continuous Separation Process for the Simultaneous Production and Direct Capture of Organic Acids.

The replacement of petrochemicals with biobased chemicals requires efficient bioprocesses, biocatalysis, and product recovery. Biocatalysis (e.g., enzyme conversion and fermentation) offers an attractive alternative to chemical processing because biocatalysis utilize renewable feedstocks under benign reaction conditions. One class of chemical products that could be produced in large volumes by biocatalysis is organic acids. However, biocatalytic reactions to produce organic acids typically result in only dilute concentrations of the product because of product inhibition and acidification that drives the reaction pH outside of the optimal range for the biocatalyst. Buffering or neutralization results in formation of the acid salt rather than the acid, which requires further processing to recover the free acid product. To address these barriers to biocatalytic organic acid production, we developed the "separative bioreactor" based on resin wafer electrodeionization, which is an electro-deionization platform that uses resin wafers fabricated from ion exchange resins. The separative bioreactor simultaneously separates the organic acid from the biocatalyst as it is produced, thus it avoids product inhibition enhancing reaction rates. In addition, the separative bioreactor recovers the product in its acid form to avoid neutralization. The instantaneous separation of acid upon formation in the separative bioreactor is one of the first truly one-step systems for producing organic acids. The separative bioreactor was demonstrated with two systems. In the first demonstration, the enzyme glucose fructose oxidoreductase (GFOR) was immobilized in the reactor and later regenerated in situ. GFOR produced gluconic acid (in its acid form) continuously for 7 days with production rates up to 1000 mg/L/hr at >99% product recovery and GFOR reactivity >30mg gluconic acid/mg GFOR/hour. In the second demonstration, the E. coli strain CSM1 produced lactic acid for up to 24 hours with a productivity of >200 mg/L/hr and almost 100% product recovery.

Bacterial expression strategies for human angiogenesis proteins.

We outline an expression strategy using Escherichia coli to obtain soluble components of a selected group of human proteins implicated in angiogenesis. These targets represent a heterogeneous group of proteins which for expression purposes were separated into cytoplasmic and helical membrane protein categories. Target selection was refined using a bioinformatic approach to generate a list of 50 experimental targets. A group consisting of forty-four cytoplasmic and signal-containing protein targets were amplified and cloned into multiple expression vectors. For this target category, we obtained 48% soluble expression products. In addition, we used a domain expression approach for six high molecular weight proteins predicted to contain membrane spanning helices to obtain soluble domain products. These results validate the utility of a bioinformatically driven high throughput approach to increase the number of soluble proteins or protein domains which can be used for multiple downstream applications.

DNA from uncultured organisms as a source of 2,5-diketo-D-gluconic acid reductases.

Total DNA of a population of uncultured organisms was extracted from soil samples, and by using PCR methods, the genes encoding two different 2,5-diketo-D-gluconic acid reductases (DKGRs) were recovered. Degenerate PCR primers based on published sequence information gave internal gene fragments homologous to known DKGRs. Nested primers specific for the internal fragments were combined with random primers to amplify flanking gene fragments from the environmental DNA, and two hypothetical full-length genes were predicted from the combined sequences. Based on these predictions, specific primers were used to amplify the two complete genes in single PCRs. These genes were cloned and expressed in Escherichia coli. The purified gene products catalyzed the reduction of 2,5-diketo-D-gluconic acid to 2-keto-L-gulonic acid. Compared to previously described DKGRs isolated from Corynebacterium spp., these environmental reductases possessed some valuable properties. Both exhibited greater than 20-fold-higher kcat/Km values than those previously determined, primarily as a result of better binding of substrate. The Km values for the two new reductases were 57 and 67 microM, versus 2 and 13 mM for the Corynebacterium enzymes. Both environmental DKGRs accepted NADH as well as NADPH as a cosubstrate; other DKGRs and most related aldo-keto reductases use only NADPH. In addition, one of the new reductases was more thermostable than known DKGRs.

Expression of a highly toxic protein, Bax, in Escherichia coli by attachment of a leader peptide derived from the GroES cochaperone.

Expression of the human apoptosis modulator protein Bax in Escherichia coli is highly toxic, resulting in cell lysis at very low concentrations (Asoh, S., et al., J. Biol. Chem. 273, 11384-11391, 1998). Attempts to express a truncated form of murine Bax in the periplasm by using an expression vector that attached the OmpA signal sequence to the protein failed to alleviate this toxicity. In contrast, attachment of a peptide based on a portion of the E. coli cochaperone GroES reduced Bax's toxicity significantly and allowed good expression. The peptide, which was attached to the N-terminus, included the amino acid sequence of the mobile loop of GroES that has been demonstrated to interact with the chaperonin, GroEL. Under normal growth conditions, expression of this construct was still toxic, but generated a small amount of detectable recombinant Bax. However, when cells were grown in the presence of 2% ethanol, which stimulated overproduction of the molecular chaperones GroEL and DnaK, toxicity was reduced and good overexpression occurred. Two-dimensional gel electrophoresis analysis showed that approximately 15-fold more GroES-loop-Bax was produced under these conditions than under standard conditions and that GroEL and DnaK were elevated approximately 3-fold.

Mutation of the ptsG gene results in increased production of succinate in fermentation of glucose by Escherichia coli.

Escherichia coli NZN111 is blocked in the ability to grow fermentatively on glucose but gave rise spontaneously to a mutant that had this ability. The mutant carries out a balanced fermentation of glucose to give approximately 1 mol of succinate, 0. 5 mol of acetate, and 0.5 mol of ethanol per mol of glucose. The causative mutation was mapped to the ptsG gene, which encodes the membrane-bound, glucose-specific permease of the phosphotransferase system, protein EIICB(glc). Replacement of the chromosomal ptsG gene with an insertionally inactivated form also restored growth on glucose and resulted in the same distribution of fermentation products. The physiological characteristics of the spontaneous and null mutants were consistent with loss of function of the ptsG gene product; the mutants possessed greatly reduced glucose phosphotransferase activity and lacked normal glucose repression. Introduction of the null mutant into strains not blocked in the ability to ferment glucose also increased succinate production in those strains. This phenomenon was widespread, occurring in different lineages of E. coli, including E. coli B.

A novel fermentation pathway in an Escherichia coli mutant producing succinic acid, acetic acid, and ethanol.

Escherichia coli strain NZN111, which is unable to grow fermentatively because of insertional inactivation of the genes encoding pyruvate: formate lyase and the fermentative lactate dehydrogenase, gave rise spontaneously to a chromosomal mutation that restored its ability to ferment glucose. The mutant strain, named AFP111, fermented glucose more slowly than did its wild-type ancestor, strain W1485, and generated a very different spectrum of products. AFP111 produced succinic acid, acetic acid, and ethanol in proportions of approx 2:1:1. Calculations of carbon and electron balances accounted fully for the observed products; 1 mol of glucose was converted to 1 mol of succinic acid and 0.5 mol each of acetic acid and ethanol. The data support the emergence in E. coli of a novel succinic acid:acetic acid:ethanol fermentation pathway.

Production of succinic acid through overexpression of NAD(+)-dependent malic enzyme in an Escherichia coli mutant.

NAD(+)-dependent malic enzyme was cloned from the Escherichia coli genome by PCR based on the published partial sequence of the gene. The enzyme was overexpressed and purified to near homogeneity in two chromatographic steps and was analyzed kinetically in the forward and reverse directions. The Km values determined in the presence of saturating cofactor and manganese ion were 0.26 mM for malate (physiological direction) and 16 mM for pyruvate (reverse direction). When malic enzyme was induced under appropriate culture conditions in a strain of E. coli that was unable to ferment glucose and accumulated pyruvate, fermentative metabolism of glucose was restored. Succinic acid was the major fermentation product formed. When this fermentation was performed in the presence of hydrogen, the yield of succinic acid increased. The constructed pathway represents an alternative metabolic route for the fermentative production of dicarboxylic acids from renewable feedstocks.

Expression of Ascaris suum malic enzyme in a mutant Escherichia coli allows production of succinic acid from glucose.

The malic enzyme gene of Ascaris suum, was cloned into the vector pTRC99a in two forms encoding alternative amino-termini. The resulting plasmids, pMEA1 and pMEA2, were introduced into Escherichia coli NZN111, a strain that is unable to grow fermentatively because of inactivation of the genes encoding pyruvate dissimilation. Induction of pMEA1, which encodes the native animoterminus, gave better overexpression of malic enzyme, approx 12-fold compared to uninduced cells. Under the appropriate culture conditions, expression of malic enzyme allowed the fermentative dissimilation of glucose by NZN111. The major fermentation product formed in induced cultures was succinic acid.

Enhanced production of succinic acid by overexpression of phosphoenolpyruvate carboxylase in Escherichia coli.

Fermentative production of succinic acid from glucose by Escherichia coli was significantly increased by overexpression of phosphoenolpyruvate carboxylase. In contrast, overexpression of phosphoenolpyruvate carboxykinase had no effect. Under optimized conditions, induction of the carboxylase resulted in a 3.5-fold increase in the concentration of succinic acid, making succinic acid the major fermentation product by weight.

Stringency of substrate specificity of Escherichia coli malate dehydrogenase.

Malate dehydrogenase and lactate dehydrogenase are members of the structurally and functionally homologous family of 2-ketoacid dehydrogenases. Both enzymes display high specificity for their respective keto substrates, oxaloacetate and pyruvate. Closer analysis of their specificity, however, reveals that the specificity of malate dehydrogenase is much stricter and less malleable than that of lactate dehydrogenase. Site-specific mutagenesis of the two enzymes in an attempt to reverse their specificity has met with contrary results. Conversion of a specific active-site glutamine to arginine in lactate dehydrogenase from Bacillus stearothermophilus generated an enzyme that displayed activity toward oxaloacetate equal to that of the native enzyme toward pyruvate (H. M. Wilks et al. (1988) Science 242, 1541-1544). We have constructed a series of mutants in the mobile, active site loop of the Escherichia coli malate dehydrogenase that incorporate the complementary change, conversion of arginine 81 to glutamine, to evaluate the role of charge distribution and conformational flexibility within this loop in defining the substrate specificity of these enzymes. Mutants incorporating the change R81Q all had reversed specificity, displaying much higher activity toward pyruvate than to the natural substrate, oxaloacetate. In contrast to the mutated lactate dehydrogenase, these reversed-specificity mutants were much less active than the native enzyme. Secondary mutations within the loop of the E. coli enzyme (A80N, A80P, A80P/M85E/D86T) had either no or only moderately beneficial effects on the activity of the mutant enzyme toward pyruvate. The mutation A80P, which can be expected to reduce the overall flexibility of the loop, modestly improved activity toward pyruvate. The possible physiological relevance of the stringent specificity of malate dehydrogenase was investigated. In normal strains of E. coli, fermentative metabolism was not affected by expression of the mutant malate dehydrogenase. However, when expressed in a strain of E. coli unable to ferment glucose, the mutant enzyme restored growth and produced lactic acid as the sole fermentation product.

The multisubunit active site of fumarase C from Escherichia coli.

The crystal structure of the tetrameric enzyme, fumarase C from Escherichia coli, has been determined to a resolution of 2.0 A. A tungstate derivative used in the X-ray analysis is a competitive inhibitor and places the active site of fumarase in a region which includes atoms from three of the four subunits. The polypeptide conformation is similar to that of delta-crystallin and is comprised of three domains. The central domain, D2, is a unique five-helix bundle. The association of the D2 domains results in a tetramer which has a core of 20 alpha-helices. The other two domains, D1 and D3, cap the helical bundle on opposite ends giving both the single subunit and the tetramer a dumbbell-like appearance. Fumarase C has sequence homology to the eukaryotic fumarases, aspartase, arginosuccinate lyase, adenylosuccinate lyase and delta-crystallin.

Oxidation of deuterated compounds by high specific activity methane monooxygenase from Methylosinus trichosporium. Mechanistic implications.

Hydrocarbon oxidations catalyzed by methane monooxygenase purified to high specific activity from the type II methanotroph Methylosinus trichosporium OB3b were compared to the same reactions catalyzed by methane monooxygenase from the type I methanotroph Methylococcus capsulatus Bath and liver microsomal cytochrome P-450. The two methane monooxygenases produced nearly identical product distributions, in accord with physical studies of the enzymes which have shown them to be very similar. The products obtained from the oxidation of a series of deuterated substrates by the M. trichosporium methane monooxygenase were very similar to those reported for the same reaction catalyzed by liver microsomal cytochrome P-450, suggesting that the enzymes use similar mechanisms. However, differences in the product distributions and other aspects of the reactions indicated the mechanisms are not identical. Methane monooxygenase epoxidized propene in D2O and d6-propene in H2O without exchange of substrate protons or deuterons with solvent, in contrast to cytochrome P-450 (Groves, J. T., Avaria-Neisser, G. E., Fish, K. M., Imachi, M., and Kuczkowski, R. L. (1986) J. Am. Chem. Soc. 108, 3837-3838), suggesting that the mechanism of epoxidation of olefins by methane monooxygenase differs at least in part from that of cytochrome P-450. Hydroxylation of alkanes by methane monooxygenase revealed close similarities to hydroxylations by cytochrome P-450. Allylic hydroxylation of 3,3,6,6-d4-cyclohexene occurred with approximately 20% allylic rearrangement in the case of methane monooxygenase, whereas 33% was reported for this reaction catalyzed by cytochrome P-450 (Groves, J. T., and Subramanian, D. V. (1984) J. Am. Chem. Soc. 106, 2177-2181). Similarly, hydroxylation of exo,exo,exo,exo-2,3,5,6-d4-norbornane by methane monooxygenase occurred with epimerization, but to a lesser extent than reported for cytochrome P-450 (Groves, J. T., McClusky, G. A., White, R. E., and Coon, M. J. (1978) Biochem. Biophys. Res. Commun. 81, 154-160). A large intramolecular isotope effect, kH,exo/kD,exo greater than or equal to 5.5, was calculated for this reaction. However, the intermolecular kinetic isotope effect on Vm for methane oxidation was small, suggesting that steps other than C-H bond breakage were rate limiting in the overall enzymatic reaction. Similar isotope effects have been observed for cytochrome P-450. These observations indicate a stepwise mechanism of hydroxylation for methane monooxygenase analogous to that proposed for cytochrome P-450.(ABSTRACT TRUNCATED AT 400 WORDS)

Methane monooxygenase catalyzed oxygenation of 1,1-dimethylcyclopropane. Evidence for radical and carbocationic intermediates.

Methane monooxygenase catalyzes the oxygenation of 1,1-dimethylcyclopropane in the presence of O2 and NADH to (1-methylcyclopropyl)methanol (81%), 3-methyl-3-buten-1-ol (6%), and 1-methyl-cyclobutanol (13%). Oxygenation by 18O2 using the purified enzyme proceeds with incorporation of 18O into the products. Inasmuch as methane monooxygenase catalyzes the insertion of O from O2 into a carbon-hydrogen bond of alkanes, (1-methylcyclopropyl)methanol appears to be a conventional oxygenation product. 3-Methyl-3-buten-1-ol is a rearrangement product that can be rationalized on the basis that enzymatic oxygenation of 1,1-dimethylcyclopropane proceeds via the (1-methylcyclopropyl)carbinyl radical, which is expected to undergo rearrangement with ring opening to the homoallylic 3-methyl-3-buten-1-yl radical in competition with conventional oxygenation. Oxygenation of the latter radical gives 3-methyl-3-buten-1-ol. 1-Methylcyclobutanol is a ring-expansion product, whose formation is best explained on the basis that the 1-methylcyclobutyl tertiary carbocation is an oxygenation intermediate. This cation would result from rearrangements of carbocations derived by one-electron oxidation of either radical intermediate. The fact that both 3-methyl-3-buten-1-ol and 1-methylcyclobutanol are produced suggests that the oxygenation mechanism involves both radical and carbocationic intermediates. Radicals and carbocations can both be intermediates if they are connected by an electron-transfer step. A reasonable reaction sequence is one in which the cofactor (mu-oxo)diiron reacts with O2 and two electrons to generate a hydrogen atom abstracting species and an oxidizing agent. The hydrogen-abstracting species might be the enzymic radical or another species generated by the iron complex and O2.(ABSTRACT TRUNCATED AT 250 WORDS)

Structure of a methanofuran derivative found in cell extracts of Methanosarcina barkeri.

Cell extracts prepared from cells of Methanosarcina barkeri grown on hydrogen and carbon dioxide, acetate, or methanol contain a coenzyme structurally related to methanofuran. This modified coenzyme was highly purified and its structure assigned as 4-[N-(gamma-L-glutamyl-gamma-L-glutamyl-gamma-L-glutamyl-gamma-L-glutamy l)-p- (beta-amino-ethyl)phenoxymethyl]-2-(aminomethyl)furan. The key structural evidence was obtained by high-resolution fast atom bombardment-mass spectrometry and 1H NMR spectroscopy. Quantitative analysis of the hydrolytic fragments of the coenzyme supported the assigned structure. We propose that this coenzyme be called methanofuran-b.

Incorporation of coenzyme M into component C of methylcoenzyme M methylreductase during in vitro methanogenesis.

Reduction of the methyl group of [methyl-3H,thio-35S]2-methylthioethanesulfonic acid to methane by a reconstituted enzyme system resulted in a slow incorporation of [thio-35S]2-mercaptoethanesulfonic acid (HS-CoM) into component C of the methylreductase system. Only 35S label was associated with component C. The ratio of incorporated HS-CoM to component C was 1.96 to 1. The ratio of HS-CoM to factor F430, the nickel-containing cofactor of component C, was 1.18 to 1. Extraction of factor F430 from the protein resulted in the release of 62 +/- 8% of the 35S label, but the label was not covalently bound to F430. The incorporation of label into component C was coupled to methyl group reduction; no label was found associated with component C from a reconstituted reaction containing unlabeled 2-methylthioethanesulfonic acid and [thio-35S]HS-CoM.

Synthesis of 7-mercaptoheptanoylthreonine phosphate and its activity in the methylcoenzyme M methylreductase system.

The structure of component B of the methylcoenzyme M methylreductase of Methanobacterium thermoautotrophicum was recently assigned as 7-mercaptoheptanoylthreonine phosphate (HS-HTP) (Noll, K. M., Rinehart, K. L., Jr., Tanner, R.S., and Wolfe, R.S. (1986) (Proc. Natl. Acad. Sci. U.S.A. 83, 4238-4242). We report here the chemical synthesis and biochemical activity of this compound. Thiourea and 7-bromoheptanoic acid were used to to synthesize 7,7'-dithiodiheptanoic acid. This disulfide was then condensed with DL-threonine phosphate using N-hydroxysuccinimide and dicyclohexylcarbodiimide. The product was reduced with dithiothreitol to give HS-HTP. It could be oxidized in air in the presence of 2-mercaptoethanol to give the compound as it was isolated from cell extracts. The resulting product was identical to the authentic compound by 1H NMR spectroscopy, mass spectrometry, and coelution using high performance liquid chromatography. The synthetic compound is active in the in vitro methanogenic assay at concentrations comparable to the authentic compound. This confirms the structure of component B as HS-HTP and provides a means to synthesize quantities sufficient for studies of the methylreductase system.

The role of formylmethanofuran: tetrahydromethanopterin formyltransferase in methanogenesis from carbon dioxide.

Formylmethanofuran: tetrahydromethanopterin formyltransferase was purified to electrophoretic homogeneity from cells of Methanobacterium thermoautotrophicum. The enzyme is a tetramer of similar or identical subunits (Mr = 41,000). The equilibrium favors transfer of the formyl group to tetrahydromethanopterin (H4MPT) at physiological pH. The product of formyl transfer by the purified enzyme was shown by a number of criteria to be 5-formyl-H4MPT, as opposed to 10-formyl-H4MPT or 5,10-methenyl-H4MPT. Reconstitution of a portion of the methanogenic C1 cycle was effected by combining purified formyltransferase, methenyl-H4MPT cyclohydrolase, formylmethanofuran, and H4MPT to give methenyl-H4MPT. Additional reconstitution experiments established that the formyltransferase is an essential enzyme for the conversion of carbon dioxide to methane. In conjunction with previously published data (Donnelly, M.I., Escalante-Semerena, J.C., Rinehart, K. L., Jr., and Wolfe, R.S. (1985) Arch. Biochem. Biophys. 242, 430-439), these data substantiate the role of 5-formyl-H4MPT as an intermediate of methanogenesis.

Purification and properties of the 5,10-methenyltetrahydromethanopterin cyclohydrolase from Methanobacterium thermoautotrophicum.

The 5,10-methenyltetrahydromethanopterin cyclohydrolase of Methanobacterium thermoautotrophicum was purified 128-fold to homogeneity. The enzyme had a subunit Mr of 41,000 as indicated by sodium dodecyl sulfate-polyacrylamide gel electrophoresis. From high-performance size exclusion chromatography of the native protein, an Mr of 82,000 was determined, suggesting a dimer of identical subunits. The enzyme was inhibited by 10-formyltetrahydromethanopterin and stimulated by Mg2+. Evaluation of the reaction equilibrium indicated that the methenyl derivative was favored over 5-formyltetrahydromethanopterin, with a much higher equilibrium constant than for the analogous reaction of tetrahydrofolate derivatives. Folate derivatives did not serve as substrates for this enzyme.

Coenzyme F420 dependence of the methylenetetrahydromethanopterin dehydrogenase of Methanobacterium thermoautotrophicum.

To identify the electron acceptor of the methylenetetrahydromethanopterin dehydrogenase of Methanobacterium thermoautotrophicum, we have purified the enzyme to homogeneity. The purified enzyme is absolutely dependent on coenzyme F420 (a 7,8-didemethyl-8-hydroxy-5-deazariboflavin derivative) for activity. Several alternative electron acceptors are ineffectual in the reaction. Changes in the absorption spectra of reaction mixtures indicate that 1.1 mol of coenzyme F420 is reduced per mol of substrate oxidized. The reaction is reversible and the equilibrium favors oxidation of methylenetetrahydromethanopterin.