Jianxin Bai

A new member of the short-chain dehydrogenases/reductases superfamily: Purification, characterization and substrate specificity of a recombinant carbonyl reductase from Pichia stipitis

A novel short-chain dehydrogenases/reductases superfamily (SDRs) reductase (PsCR) from Pichia stipitis that produced ethyl (S)-4-chloro-3-hydroxybutanoate with greater than 99% enantiomeric excess, was purified to homogeneity using fractional ammonium sulfate precipitation followed by DEAE-Sepharose chromatography. The enzyme purified from recombinant Escherichia coli had a molecular mass of about 35 kDa on SDS-PAGE and only required NADPH as an electron donor. The K(m) value of PsCR for ethyl 4-chloro-3-oxobutanoate was 4.9 mg/mL and the corresponding V(max) was 337 micromol/mg protein/min. The catalytic efficiency value was the highest ever reported for reductases from yeasts. Moreover, PsCR exhibited a medium-range substrate spectrum toward various keto and aldehyde compounds, i.e., ethyl-3-oxobutanoate with a chlorine substitution at the 2 or 4-position, or alpha,beta-diketones. In addition, the activity of the enzyme was strongly inhibited by SDS and beta-mercaptoethanol, but not by ethylene diamine tetra acetic acid.

Selective separation of biobutanol from acetone-butanol-ethanol fermentation broth by means of sorption methodology based on a novel macroporous resin.

The traditional distillation method for recovery of butanol from fermentation broth is an energy‐intensive process. Separation of butanol based on adsorption methodology has advantages in terms of biocompatibility and stability, as well as economy, and therefore gains much attention. However, the application of the commercial adsorbents in the integrated acetone–butanol–ethanol (ABE) fermentation process is restricted due to the low recovery (less than 85%) and the weak capability of enrichment in the eluent (3–4 times). In this study, we investigated the sorption properties of butanol onto three kinds of adsorbents with different polarities developed in our laboratory, that is, XD‐41, H‐511, and KA‐I resin. The sorption behaviors of single component and ABE ternary mixtures presented in the fermentation broths on KA‐I resin were investigated. KA‐I resin had higher affinity for butanol than for acetone, ethanol, glucose, acetic acid, and butyric acid. Multicomponent ABE sorption on KA‐I resin was modeled using a single site extended Langmuir isotherm model. In a desorption study, all the adsorbed components were desorbed in one bed volume of methanol, and the recovery of butanol from KA‐I resin was 99.7%. The concentration of butanol in the eluent was increased by a factor of 6.13. In addition, KA‐I resin was successfully regenerated by two bed volumes of water. Because of its quick sorption, high sorption capacity, low cost, and ease of desorption and regeneration, KA‐I resin exhibits good potential for compatibility with future ABE fermentation coupled with in situ recovery product removal techniques.

Experimental and Modeling Studies on the Sorption Breakthrough Behaviors of Butanol from Aqueous Solution in a Fixed-bed of KA-I Resin

Removal of biobutanol from acetone-butanolethanol (ABE) fermentation broth can be achieved by fixed-bed sorption by means of KA-I resin, and the relevant breakthrough curves would provide much valuable information to help design a continuous fixed-bed sorption process in field application. In the present study, the effects of several important design parameters, i.e., initial butanol concentration (Cf: 3.0 ∼ 30.0 g/L), inlet flow rate (Qf: 0.5 ∼ 5.5 mL/min) and adsorbent bed height (Z: 4.2 ∼ 18.0 cm), on the adsorption breakthrough curves of KA-I resin in a fixed-bed column were investigated. It was found that the amount of adsorbed butanol at breakthrough point was increased with an increase in the value of Cf and Z; and with decrease in the value of Qf. However, the maximum sorption capacities of butanol at saturated point were basically unchanged. Three well-established fixed-bed adsorption models, namely Thomas, Yoon-Nelson and Adams-Bohart, were applied to predict the breakthrough curves and to determine the characteristic parameters of fixed-bed column, which are the basis for the process design at a real scale. Good agreement between the theoretical breakthrough curves and the experimental result were observed using Thomas and Yoon-Nelson models.

Enhanced cyclic adenosine monophosphate production by Arthrobacter A302 through rational redistribution of metabolic flux.

Cyclic adenosine monophosphate (cAMP) was synthesized through the purine salvage synthesis pathway by Arthrobacter A302. Results showed that hypoxanthine was the best of the precursors, and the cAMP concentration reached 4.06 g/L. For inhibition of the glycolytic pathway, sodium fluoride was found the optimal effector, which was further studied on cAMP production. With the addition of 0.4 g/L of sodium fluoride, the maximal cAMP concentration reached 11.04 g/L, and the concentrations of lactic acid, alpha-ketoglutarate and citric acid were decreased by 77%, 86% and 76%, respectively. Meanwhile, the specific activities of glyceraldehyde 3-phosphate dehydrogenase, phosphofructokinase and pyruvate kinase were decreased by 66%, 61%, and 46%, respectively. By contrast the activity of 6-phosphoglucose dehydrogenase was increased by 100%, which demonstrated the redistribution of metabolic flux. This is the first study to reveal the regulatory mechanisms of different effectors on cAMP production among the EMP pathway, HMP pathway and TCA cycle.

Effect of NH4+ and glycerol on cytidine 5′-diphosphocholine synthesis in Saccharomyces cerevisiae.

Both stimulation of ammonium ion on the glycolytic flux and regulation by glycerol of enzymes in Kennedy pathway for cytidine diphosphate choline production in S. cerevisiae were studied. The conventional transformation course featured four stages. Firstly, CMP and choline chloride were phosphorylated and CDP-choline was formed rapidly; secondly, the rate of CDP-choline formation declined and CMP was not detected in the mixture; thirdly, CMP was released and the CDP-choline concentration reached a peak; Fourthly, the compound concentrations did not practically changes eventually. Using the central composite design, the concentration, yield, and utilization efficiency of energy reached 24.7 mmol/L, 82.3% and 10.6%, with 30 mmol/L of ammonium ion and 1% (V/V) of glycerol, respectively. Ammonium ion not only strengthened the glycolytic pathway, but also coordinated the reaction rate between the glycolytic pathway and the Kennedy pathway. Glycerol alleviated the activity decrease of the key enzymes in the mixture.

Optimization and Validation of a GC–FID Method for the Determination of Acetone-Butanol-Ethanol Fermentation Products

An improved, simple gas chromatography-flame ionization detection (GC-FID) method was developed for measuring the products of acetone-butanol-ethanol (ABE) fermentation and the combined fermentation/separation processes. The analysis time per sample was reduced to less than 10 min compared to those of a conventional GC-FID (more than 20 min). The behavior of the compounds in temperature-programmed gas chromatographic runs was predicted using thermodynamic parameters derived from isothermal runs. The optimum temperature programming condition was achieved when the resolution for each peak met the analytical requirement and the analysis time was shortest. With the exception of acetic acid, the detection limits of the presented method for various products were below 10 mg/L. The repeatability and intermediate precision of the method were less than 10% (relative standard deviation). Validation and quantification results demonstrated that this method is a sensitive, reliable and fast alternative for conventional investigation of the adsorption-coupled ABE fermentation process.

Effect of ribose, xylose, aspartic acid, glutamine and nicotinic acid on ethyl (S)-4-chloro-3-hydroxybutanoate synthesis by recombinant Escherichia coli.

Most reductases which belong to the short chain dehydrogenase/reductase (SDR) superfamily require NAD (P) H for activity. Addition of this cofactor was still necessary for the production of ethyl (S)-4-chloro-3-hydroxybutanoate by Escherichia coli even when a cofactor regeneration system was constructed by co-expressing carbonyl reductase from Pichia stipitis (PsCRI) and glucose dehydrogenase from Bacillus megaterium (BmGDH). In an attempt to reduce dependence on the expensive cofactor, compounds directly or indirectly involved in NADP synthesis were added to the medium. Only glutamine and xylose enhanced the content of intracellular NADP (H) and the concentration of product. The concentration and yield of (S)-CHBE reached 730 mM and 48.7%, with 30 g/L of glutamine and 40 g/L of xylose, a 2.6-fold increase over the control without the addition of the two compounds.

Production of cyclic adenosine-3′,5′-monophosphate by whole cell catalysis using recombinant Escherichia coli overexpressing adenylate cyclase

Adenylate cyclase (EC 4.6.1.1) catalyzes the formation of cyclic adenosine-3′,5′-monophosphate (cAMP) from adenosine 5′-triphosphate (ATP). Recombinant Escherichia coli overexpressing adenylate cyclase was used to synthesize cAMP by whole cell catalysis. Some key parameters were examined during the catalytic process, while pH and Mg2+ were found to influence cAMP production significantly. Optimum conditions were pH 8.52 and 30 °C with 77.2 mM Mg2+ in 100 mM Tris-HCl buffer, including 0.25% Triton-X 100 as detergent and 30 mM pyruvate sodium as enzyme activator for 6 h. 14.93 g/L of cAMP was produced with a conversion rate of 91.5%. The current work provided a potential way for the industrial production of cAMP.