Sorbitol and Gluconate Production in a Hollow Fibre Membrane Reactor by Immobilized Zymomonas Mobilis

This study describes the results of a hollow fibre membrane reactor with immobilized treated cells of Zymomonas mobilis which produced sorbitol and gluconic acid continuously from fructose and glucose respectively. A productivity of 10–20 g sorbitol · L^-1 · h^-1 and 10–20 gluconate · L^-1 · h^-1 (based on total bioreactor volume) from a feed of 100 g · L^-1 each of glucose and fructose was possible at high dilution rates. Kinetic parameters describing the reaction rate of treated cells in batch reactors were used to analyse the performance of the hollow fibre membrane reactor employing significant convective mass transfer. No significant mass transfer limitation was apparent.     

Sorbitol and Gluconate Production in a Hollow Fibre Membrane Reactor by Immobilized Zymomonas Mobilis

This study describes the results of a hollow fibre membrane reactor with immobilized treated cells of Zymomonas mobilis which produced sorbitol and gluconic acid continuously from fructose and glucose respectively. A productivity of 10-20 g sorbitol · L^-1 · h^-1 and 10-20 gluconate · L^-1 · h^-1 (based on total bioreactor volume) from a feed of 100 g · L^-1 each of glucose and fructose was possible at high dilution rates. Kinetic parameters describing the reaction rate of treated cells in batch reactors were used to analyse the performance of the hollow fibre membrane reactor employing significant convective mass transfer. No significant mass transfer limitation was apparent.     

Continuous Production of l-Alanine with NADH Regeneration by a Nanofiltration Membrane Reactor

A conjugated enzyme system, alanine dehydrogenase (AIDH) for stereospecific reduction of pyruvate to l-alanine and glucose dehydrogenase (GDH) for regeneration of NADH, were coimmobilized in a nanofiltration membrane bioreactor (NFMBR) for the continuous production of l-alanine from pyruvate with NADH regeneration. Since pyruvate was proved to be unstable at neutral pH, it was kept under acidic conditions and supplied to NFMBR separately from the other substrates. As 0.2 m pyruvate in HCl solution (pH 4), 10 mm NAD, 0.2 m glucose, and 0.2 m NH₄Cl in 0.5 m Tris buffer (pH 8) were continuously supplied to NFMBR with immobilized AIDH (100 U/ml) and GDH (140 U/ml) at the retention time of 80 min, the maximum conversion, reactor productivity, and NAD regeneration number were 100%, 320 g/liter/d, and 20,000, respectively. To avoid the effect of pyruvate instability, a consecutive reaction system, lactate dehydrogenase (l-LDH) and AIDH, was also used. In this system, the l-LDH provides pyruvate, the substrate for the AIDH reaction, from l-lactate regenerating NADH simultaneously, so the pyruvate could be consumed as soon as it was produced. As 0.2 m l-lactate, 10 mm NAD, 0.2 m NH₄Cl in 0.5 m Tris buffer (pH 8) were continuously supplied to NFMBR with immobilized l-LDH (100 U/ml) and AIDH (100 U/ml) at the retention time of 160 min, the maximum conversion, reactor productivity, and the NAD regeneration number were 100%, 160 g/Iiter/d, and 20,000, respectively.     

Stirred Tank Two-Liquid Phase Biocatalytic Reactor Studies: Kinetics, Evaluation and Modelling of Substrate Mass Transfer

Kinetic measurements of the benzyl acetate hydrolysis by pig liver esterase in a two-liquid phase stirred tank reactor were made at a variety of aqueous phase enzyme concentrations and stirrer speeds. All experiments were performed in an inverted liquid-liquid system at a high phase ratio. The results were explained in terms of the aqueous phase bulk reaction model developed from previous Lewis cell studies. An algorithm is presented for the indirect measurement of the substrate mass transfer coefficient and consequently a model was developed to predict reaction rates. While the model describes the kinetics effectively, and could therefore be used to predict reactor behaviour, no difference was observed between kinetic measurements made at a stirrer speed of 750 and 1000 rpm.     

Analysis of the Microbial Community in an Acidic Hollow-Fiber Membrane Biofilm Reactor (Hf-MBfR) Used for the Biological Conversion of Carbon Dioxide to Methane

Hydrogenotrophic methanogens can use gaseous substrates, such as H₂ and CO₂, in CH₄ production. H₂ gas is used to reduce CO₂. We have successfully operated a hollow-fiber membrane biofilm reactor (Hf-MBfR) for stable and continuous CH₄ production from CO₂ and H₂. CO₂ and H₂ were diffused into the culture medium through the membrane without bubble formation in the Hf-MBfR, which was operated at pH 4.5–5.5 over 70 days. Focusing on the presence of hydrogenotrophic methanogens, we analyzed the structure of the microbial community in the reactor. Denaturing gradient gel electrophoresis (DGGE) was conducted with bacterial and archaeal 16S rDNA primers. Real-time qPCR was used to track changes in the community composition of methanogens over the course of operation. Finally, the microbial community and its diversity at the time of maximum CH₄ production were analyzed by pyrosequencing methods. Genus Methanobacterium, related to hydrogenotrophic methanogens, dominated the microbial community, but acetate consumption by bacteria, such as unclassified Clostridium sp., restricted the development of acetoclastic methanogens in the acidic CH₄ production process. The results show that acidic operation of a CH₄ production reactor without any pH adjustment inhibited acetogenic growth and enriched the hydrogenotrophic methanogens, decreasing the growth of acetoclastic methanogens.     

Phenol removal from hypersaline wastewaters in a Membrane Biological Reactor (MBR): operation and microbiological characterisation

In this study, two Membrane Biological Reactors (MBR) with submerged flat membranes, one at lab-scale conditions and the other at pilot-plant conditions, were operated at environmental temperature to treat an industrial wastewater characterised by low phenol concentrations (8-16 mg L⁻¹) and high salinity (∼150-160 mS cm⁻¹). During the operation of both reactors, the phenol loading rate was progressively increased and less than 1 mg phenol L⁻¹ was detected even at very low HRTs (0.5-0.7 days). Membrane fouling was minimized by the cross flow aeration rate inside the MBRs and by intermittent permeation. Microbial community analysis of both reactors revealed that members of the genera Halomonas and Marinobacter (gammaproteobacteria) were major components. Growth-linked phenol degradation by pure cultures of Marinobacter isolates demonstrated that this bacterium played a major role in the removal of phenol from the bioreactors.     

Factors in the Membrane Filtration of Enteroviruses

The filtration of two species of enteroviruses through membranes of porosity ranging from 50 to 220 mμ was studied. It was shown that extensive or total losses of virus may attend filtration at these porosities, apparently owing to adsorption of the virus to the membrane matrix. This could be minimized by the incorporation of serum into the virus suspension at the time of filtration, or by pretreating the membrane with serum or with a gelatin solution. It was also found that the first few drops of filtrate, even under optimal conditions, were likely to be virus-free, so that the filtration of too small a volume of virus suspension would result in a relatively great loss of titer. The degree to which these factors were critical was found to decrease with increasing pore diameter.     

Ergosterol-to-Biomass Conversion Factors for Aquatic Hyphomycetes

Fourteen strains of aquatic hyphomycete species that are common on decaying leaves in running waters were grown in liquid culture and analyzed for total ergosterol contents. Media included an aqueous extract from senescent alder leaves, a malt extract broth, and a glucose-mineral salt solution. Concentrations of ergosterol in fungal mycelium ranged from 2.3 to 11.5 mg/g of dry mass. The overall average was 5.5 mg/g. Differences among both species and growth media were highly significant but followed no systematic pattern. Stationary-phase mycelium had ergosterol contents 10 to 12% lower or higher than mycelium harvested during the growth phase, but these differences were only significant for one of four species examined. Availability of plant sterols in the growth medium had no clear effect on ergosterol concentrations in two species tested. To convert ergosterol contents determined in field samples to biomass values of aquatic hyphomycetes, a general multiplicative factor of 182 is proposed. More accurate estimates would be obtained with species-specific factors. Using these in combination with estimates of the proportion of the dominant species in a naturally established community on leaves resulted in biomass estimates that were typically 20% lower than those obtained with the general conversion factor. Improvements of estimates with species-specific factors may be limited, however, by intraspecific variability in fungal ergosterol content.     

Biocatalytic transformations in ionic liquids

Room temperature ionic liquids are non-volatile, thermally stable and highly polar; they are also moderately hydrophilic solvents. Here, we discuss their use as reaction media for biocatalysis. Enzymes of widely diverging types are catalytically active in ionic liquids or aqueous biphasic ionic liquid systems. Lipases, in particular, maintain their activity in anhydrous ionic liquid media; the (enantio)selectivity and operational stability are often better than in traditional media. The unconventional solvent properties of ionic liquids have been exploited in biocatalyst recycling and product recovery schemes that are not feasible with traditional solvent systems.     

Biocatalytic and biomimetic oxidations with vanadium

Approaches to the rational design of vanadium-based semi-synthetic enzymes and biomimetic models as catalysts for enantioselective oxidations are reviewed. Incorporation of vanadate ion into the active site of phytase (E.C. 3.1.3.8), which in vivo mediates the hydrolysis of phosphate esters, afforded a semi-synthetic peroxidase. It catalyzed the enantioselective oxidation of prochiral sulfides with H2O2 affording the S-sulfoxide, e.g. in 66% ee at quantitative conversion of thioanisole. Under the reaction conditions the semi-synthetic vanadium peroxidase was stable for more than 3 days with only a slight decrease in turnover frequency. Amongst the transition-metal oxoanions that are known to be potent inhibitors of phosphatases, only vanadate resulted in a semi-synthetic peroxidase when incorporated into phytase. In a biomimetic approach, vanadium complexes of chiral Schiff base complexes were encapsulated in the super cages of a hydrophobic zeolite Y. Unfortunately, these ship-in-a-bottle complexes afforded only racemic sulfoxide in the catalytic oxidation of thioanisole with H2O2.     

Biocatalytic dechlorination of trichloroethylene with bio-palladium in a pilot-scale membrane reactor

Trichloroethylene (TCE) is a toxic and recalcitrant groundwater pollutant. An innovative technology using microbial produced Pd(0) nanoparticles for the remediation of TCE contaminated groundwater was developed. The nanoscale bio-Pd particles were precipitated on the biomass of Shewanella oneidensis and hydrogen gas, formate, or formic acid were used as hydrogen donors. Ethane turned out to be the only organic degradation product and no intermediate chlorinated reaction products were detected. Subsequently bio-Pd was implemented in a plate membrane reactor (MR) for the treatment of water containing TCE. In a continuous MR system, containing 50 mg L(-1) bio-Pd, removal rates up to 2,515 mg TCE day(-1) g(-1) Pd were achieved with H(2) gas as hydrogen donor. The measured chloride mass balance confirmed the removal rates. This work shows that a complete, efficient and rapid removal of TCE was achieved with bio-Pd and that a MR system containing bio-Pd and supplied with hydrogen gas offers an alternative for the current remediation technologies of water contaminated with TCE.     

The Influence of Fatty Acid and Glycerol on the Kinetics of Fat Hydrolysis by Candida Rugosa Lipase in a Membrane Reactor

The kinetics of lipid-hydrolysis by Candida rugosa lipase was investigated in a membrane reactor and in an emulsion system. Two models were chosen to describe the kinetics of the enzyme:

(1) The hydrolysis of triglycerides to fatty acids was considered to be a chain reaction with the intermediary products di- and mono-glyceride; each step was assumed to be a reversible second-order reaction. The reaction rate constants were determined from batch experiments. The experimental results could be described with this model.

(2) For process optimization and control, a model based on the power law was developed. For this model, the rate of hydrolysis was measured as a function of fatty acid and glycerol concentrations. Relations for the initial rate and equilibrium ester fraction as a function of the glycerol concentration were determined. Further, the reaction rate could be described with the power-law model with a power of 1.75 in the hydrolyzable ester fraction for a wide range of glycerol concentrations. The model with power 1.75 gave much better results when compared to a similar first order model. Although simpler, the first order model can not be used. The power law model was applied in the simulation of a reactor composed of three modules. The fatty acid production rate was calculated for this reactor system as a function of the outgoing glycerol concentration at different conditions.     

UASB反应器中影响污泥颗粒化的工程因素

研究了具有不同微生物群系的接种污泥、流动方式和流速对上流式厌氧污泥床(UASB)反应器中活性污泥粒化的影响。颗粒化过程包括：微生物絮凝体的形成、亚核的形成,亚核增长和颗粒成熟四个阶段。微絮凝体的形成取决于酸化菌的作用。流体的动量传递和流体对悬浮物的剪切作用是影响亚核形成的关键性工程因素。为此提出最低流速概念,即形成污泥膨胀床的最低流速。合适的进料速率、污泥负荷、布水均匀性以及碱度控制是UASB反应器工程放大和过程控制的四大要素。     

Bacteriophage and Bacteria in a Flow Reactor

The Levin-Stewart model of bacteriophage predation of bacteria in a chemostat is modified for a flow reactor in which bacteria are motile, phage diffuse, and advection brings fresh nutrient and removes medium, cells and phage. A fixed latent period for phage results in a system of delayed reaction-diffusion equations with non-local nonlinearities. Basic reproductive numbers are obtained for bacteria and for phage which predict survival of each in the bio-reactor. These are expressed in terms of physical and biological parameters. Persistence and extinction results are obtained for both bacteria and phage. Numerical simulations are in general agreement with those for the chemostat model.     

多瑞吉在带状疱疹疼痛治疗阿片类药物转换中的应用

目的:探讨多瑞吉在带状疱疹疼痛治疗阿片类药物转换中的应用。方法:选择37例住院治疗的带状疱疹疼痛患者,年龄>45岁、VAS评分≥4分、所有病人常规抗病毒治疗、增加免疫力等常规治疗,予硬膜外腔置管间断注入消炎镇痛药物并持续泵吗啡,根据疼痛调整至止痛剂量,转换为多瑞吉贴剂后出院。疼痛控制后逐渐减药,每半个月减量半贴多瑞吉,对病人的疼痛评分、生活质量及并发症进行评估。结果:有1例病人应药物副反应出组,其余病人硬膜外泵吗啡后均在一周左右控制疼痛,等效转换为多瑞吉,定时定量减药,无疼痛反复,成瘾戒断等情况。结论:带状疱疹疼痛采用硬膜外间断注药持续泵吗啡迅速达到无痛后,转换为等效剂量的多瑞吉,定时定量减药,安全有效。     

Membrane Potentials and Ion Permeability in a Cation Exchange Membrane

The nonequilibrium electrical potentials across an artificial membrane bathed by solutions of a single salt have been measured and calculated using the Goldman-Hodgkin-Katz equation and the irreversible thermodynamic equation. The latter equation predicts the observed potential differences over a 2500-fold concentration range, while application of a modified Goldman-Hodgkin-Katz equation leads to difficulties.     

离子液体在生物催化反应中的应用

首先概括了离子液体中生物催化反应的特点;阐述了离子液体在生物催化反应中的应用进展,主要包括:蛋白酶催化的反应、脂肪酶催化的反应、氧化还原酶催化的反应以及其它酶催化的反应.离子液体通常起到了提高酶的活性或稳定性,并提高产物收率和选择性的作用;并展望了离子液体作为溶剂和共溶剂在生物催化反应中的发展前景.