Separation of dilute aqueous butanol and acetone solutions by pervaporation through liquid membranes

A simultaneous extraction-stripping process is proposed for separating volatile products from fermentation broths, it is based on pervaporation through a liquid membrane supported with a hydrophobic porous membrane. The liquid membrane prepared with oleyl alcohol was selected as the most suitable for separating volatile products resulting from acetone-butanol fermentation. The separation performance and stability of the oleyl alcohol liquid membrane were investigated by using dilute aqueous butanol and acetone solutions. The oleyl alcohol liquid membrane was found to be superior by far in both selectivity and permeability of butanol to the better known silicone rubber membrane in its high selectivity for alcohols. Using the oleyl alcohol liquid membrane, the dilute aqueous butanol solutions of around 4 g/L obtained in acetone-butanol fermentation could be concentrated up to 100 times. The stability of this liquid membrane was also quite good as long as the surface tension of the feed solution was less than the critical surface tension of the support membrane. No change in the separation performance was found after the continuous usage in a long period of 100 h.     

Production of toluene cis-glycol by Pseudomonas putida in glucose feb-batch culture

Toluene was oxidized by a mutant strain of Pseudomonas putida (strain NG1) to toluene Cis-Glycol (TCG). Product was accumulated in fed-batch cultures to concentrations (18-24 g/L) higher than hitherto achieved. In vitro activities of toluene dioxygenase from P. Putida NG1 were fivefold lower than that from the toluene-grown wild-type organism, whereas comparable activities of both catechol 2,3- and catechol 1,2-oxygenase were obtained; irreversible inhibition of toluene dioxygenase activity by TCG was shown in vitro. Ammonia deprivation during the production phase limited the growth of revertant organisms but had little effect on either the duration (25h) of the process or the final concentration of TCG achieved. The rate of glucose utilization decreased throughout the biotransformation and cell death accompanied the cessation of TCG accumulation in cultures. These changes were a consequence of TCG formation and a cooperative toxic effect was demonstrated for toluene and TCG. Adenylate energy charge values decreased from ca. 0.8 to 0.2 over the course of the biotransformation but were maintained above 0.5 in the absence of TCG. Similarly, cellular AMP levels increased dramatically during biotransformation, presumably as a consequence of RNA degradation, but were maintained at low levels in the absence of TCG. The results suggest that TCG is the mediate of a gradual deterioration in the state of the culture which leads to a loss of both in vivo and in vitro toluence dioxygenase activity and a marked decrease in culture viability.     

Distribution of heparinase covalently immobilized to agarose: Experimental and theoretical studies

An immobilized enzyme reactor has been developed to remove heparin, the anticoagulant that is required in all extracorporeal devices for patients undergoing open-heart surgery or kidney dialysis. The device uses the enzyme heparinase (EC 4.2.2.7), which is covalently linked to agarose with cyanogen bromide. A critical parameter in the development of a model for the degradation of heparin catalyzed by immobilized heparinase is the radial concentration profile of the enzyme within the agarose matrix. Experimental determinations of bound enzyme con centrations have been conducted previously for several enzyme systems using radioactive or fluorescent labels. For the development of the heparinase reactor it is necessary to use catalytically but not electrophoretically pure enzyme, and thus it is not possible to use the labeling techniques. To obtain information about the bound enzyme distribution, an experimental study of the intrinsic binding kinetics of heparinase to cyanogen bromide-activated agarose was conducted. The binding reaction was studied as a function of both the concentration of heparinase and the gel-reactive group. At conditions of functional group excess, the binding kinetics were pseudo first order in heparinase concentration with a rate constant equal to 0.12 C(c[triple chemical bond]n) (h(-1)), where C(c[triple chemical bond]n) is the gel-reactive group concentration. The reactive group concentration remained constant within the 2-4-h experiments. Competitive binding between heparinase and the protein contaminants was unimportant. A model was formulated for the immobilization procedure based on the diffusion of heparinase within the porous network and the binding kinetics as determined above. The model predicted the immobilization of heparinase to be kinetically controlled and the enzyme to distribute uniformly within the agarose matrix. These experimental techniques could be applied to predict the immobilized enzyme distribution for different enzyme systems that are not electrophoretically pure.     

Immobilized heparinase: In vitro reactor model

Heparinase immobilized to agarose has previously been shown to be useful in degrading heparin and thereby preventing thromboembolytic complications when this anticoagulant has been used in extracorporeal perfusions. The current study examined the kinetics of this immobilized enzyme. When heparinase is covalently bound to 8% agarose, the partition coefficient of heparin in the catalytic particle is 0.36 +/- 0.048 (N = 10). The immobilized enzyme has a K(m) of 0.15 +/- 0.03 mg/mL and an activation energy of 10.3 +/- 0.57 kcal/gmol (N = 5). These values are statistically indistinguishable from the values for the free enzyme. The immobilized enzyme showed a pH activity optimum between 7.0 and 7.4, compared to the optimum pH of 6.5 for the soluble enzyme. The activity optimum of immobilized heparinase with respect to salt concentration was between 0 and 0.1M. A reactor containing immobilized heparinase recirculating internally at 1300 mL/min behaved as a continuously stirred tank reactor (CSTR) when solutions at a flow rate of 120 mL/min were passed through the device. The residence time distribution was determined using blue dextran (molecular weight 2 x 10(6) daltons), which is sterically excluded from the agarose catalyst. A model of the heparinase reactor based on ideal CSTR behavior and the immobilized enzyme kinetic parameters was developed. It accurately predicted experimental conversions over a range of catalyst volumes, enzyme loadings, and substrate concentrations to within 7% in most cases and with a maximum deviation of 13%.     

Continuous production of L-phenylalanine by transamination

L-Phenylalanine was produced continuously from L-as-partate and phenylpyruvate by transaminase from a newly screened Pseudomonas putida strain. The process was carried out with an isolated enzyme in homogeneous phase in an enzyme membrane reactor and with immobilized whole cells in a stirred tank reactor, respectively. Due to the difference in transport resistance, the productivity of the free enzyme in homogeneous phase (72 mmol/L h) was about 3 times higher than the productivity achieved using immobilized cells. However, a better stability of the biocatalyst was observed with immobilized cells.     

简介《关于啮齿类进化关系的多学科分析》

<正> 啮齿类是在生存竞争中最成功的一类哺乳动物.它们一直受到实验和进化生物学家的特别关注.最近几十年来,有关现生和化石啮齿类的新资料急剧增加.特别是关于啮齿目起源,进化以及它和其它有关门类的系统关系,许多有关学科(如古生物学、胚胎学、比较解剖学、分子生物学、遗传学、细胞发生学等)从各自不同的角度提出了许多意想不到的新见解、新设想,使关于啮齿类的研究呈现出一片生气勃勃的景     

Superoxide Dismutase Activity in Needles of Norwegian Spruce Trees (Picea abies L.)

The activity of superoxide dismutase was investigated in needles of spruce trees. To obtain maximum activity, needles were homogenized in the presence of Triton X-100 and polyvinylpyrrolidone. Superoxide dismutase activity was measured in dialyzed extracts with a modified epinephrine assay (HP Misra, I Fridovich [1972] J Biol Chem 247: 3170-3175) at pH 10.2. The extracts contained 70 to 120 units of superoxide dismutase per milligram protein. One unit of superoxide dismutase was completely inhibited in the presence of 20 micromolar NaCN. On native polyacrylamide gels three electromorphs were visualized after staining for activity. All three species were sensitive to CN⁻ and H₂O₂ and were therefore assumed to be Cu/Zn-superoxide dismutases. Superoxide dismutase activity was dependent on the age of the needles and declined by approximately 25% within 3 to 4 years.     

Abscisic Acid ELISA: Organic Acid Interference

Consideration must be exercised in determination of buffers and solutions used when carrying out enzyme-linked immunosorbent assays (ELISAs). A commercial monoclonal antibody kit for abscisic acid (Idetek, Inc.) gives significant false-positives with tricarboxylic acid cycle intermediates. The organic acids or contaminants interfered with ELISA assays for ABA as indicated by deviations in the slopes of standard curves of ABA in the organic acids. The interference, in the case of α-ketoglutarate, was caused by a contaminant. Of the organic buffers tested—Tris, Tricine, and Hepes—only Hepes showed false-positive ABA. In addition, we present data indicating the presence of ABA in commercial mannitol and provide a simple procedure for removal of the ABA.     

Growth rates and assimilate partitioning in the elongation zone of tall fescue leaf blades at high and low irradiance

Tall fescue (Festuca arundinacea Schreb.) leaf blades elongated 33% faster at continuous low than at continuous high irradiance (60 versus 300 micromoles per second per square meter photosynthetic photon flux density) when temperature of the leaf elongation zone was held constant at 21°C. Increased rate of elongation was associated with a near proportional increase in length of the elongation zone (+38%). In contrast, growth in width and thickness was decreased at low irradiance, resulting in only a 12% increase in leaf area production and 5% less total growth-associated water deposition than at high irradiance. At low irradiance dry matter (DM) import into the elongation zone was 28% less, and 55% less DM was used per unit leaf area produced. DM use in synthesis of structural components (i.e. DM less water-soluble carbohydrates) was only 13% less at low irradiance, whereas water-soluble carbohydrates (WSC) deposition was 43% less. The lower rate of WSC deposition at low irradiance was associated with a higher net rate of monosaccharide deposition (+39%), whereas net deposition rates for sucrose (−27%) and fructan (−56%) were less than at high irradiance. Still, at low irradiance, net fructan accumulation accounted for 64% of WSC deposition, i.e. 25% of DM import, demonstrating the high sink strength of the leaf elongation zone.