Immobilization of an amino acid racemase for application in crystallization‐based chiral resolutions of asparagine monohydrate

Integration of racemization and a resolution process is an attractive way to overcome yield limitations in the production of pure chiral molecules. Preferential crystallization and other crystallization‐based techniques usually produce low enantiomeric excess in solution, which is a constraint for coupling with racemization. We developed an enzymatic fixed bed reactor that can potentially overcome these unfavorable conditions and improve the overall yield of preferential crystallization. Enzyme immobilization strategies were investigated on covalent‐binding supports. The amino acid racemase immobilized in Purolite ECR 8309F with a load of 35 mg‐enzyme/g‐support showed highest specific activity (approx. 500 U/g‐support) and no loss in activity in reusability tests. Effects of substrate inhibition observed for the free enzyme were overcome after immobilization. A packed bed reactor with the immobilized racemase showed good performance in steady state operation processing low enantiomeric excess inlet. Kinetic parameters from batch reactor experiments can be successfully used for prediction of packed bed reactor performance. Full conversions could be achieved for residence times above 1.1 min. The results suggest the potential of the prepared racemase reactor to be combined with preferential crystallization to improve resolution of asparagine enantiomers.     

Preparation of Fine Magnetic Particles and Application for Enzyme Immobilization

Fine magnetic particles (ferrofluid) were prepared from a co-precipitation method by oxidation of Fe²⁺ with nitrite. The particles were activated with (3-aminopropyl)triethoxysilane in toluene and the activated particles were combined with some enzymes by using glutaraldehyde. Enzyme-immobilized magnetic particles were between 4-70 nm and the size could be changed corresponding to the ratio of the amount of Fe²⁺ to that of nitrite. In the immobilization of β-glucosidase, activity yield was 83% and 168 mg protein was immobilized per g magnetite. Other enzymes or proteins could be immobilized at the level between about 70 and 200mg/g support. Immobilized β-glucosidase was stable at 4°C. Magnetic particles immobilized with β-glucosidase responded quickly to the magnetic field and “ON-OFF” control of the enzyme reaction was possible.     

Preparation of Fine Magnetic Particles and Application for Enzyme Immobilization

Fine magnetic particles (ferrofluid) were prepared from a co-precipitation method by oxidation of Fe²⁺ with nitrite. The particles were activated with (3-aminopropyl)triethoxysilane in toluene and the activated particles were combined with some enzymes by using glutaraldehyde. Enzyme-immobilized magnetic particles were between 4-70 nm and the size could be changed corresponding to the ratio of the amount of Fe²⁺ to that of nitrite. In the immobilization of β-glucosidase, activity yield was 83% and 168 mg protein was immobilized per g magnetite. Other enzymes or proteins could be immobilized at the level between about 70 and 200mg/g support. Immobilized β-glucosidase was stable at 4°C. Magnetic particles immobilized with β-glucosidase responded quickly to the magnetic field and “ON-OFF” control of the enzyme reaction was possible.     

Immobilization of native and dextran-free dextransucrases from Leuconostoc mesenteroides NRRL B-512F for the synthesis of glucooligosaccharides

Dextransucrase from Leuconostoc mesenteroides NRRL B-512F was immobilized using two different methods: covalent attachment to activated silica and entrapment in calcium alginate. For immobilization on silica, native enzyme and dextran-free enzyme were compared. However, the entrapment in calcium alginate beads gave the best results in terms of immobilization yield and stability. This biocatalyst was employed in the acceptor reaction with maltose showing similar glucooligosaccharide production than the native enzyme but increased operational stability.     

Immobilization of levan fructotransferase for the production of di-fructose anhydride from levan

Levan fructotransferase (LFTase) from Arthrobacter ureafaciens K2032 was immobilized on various carriers of which Chitopearl BCW2501 beads showed the higher activity of 320 U g^–1 for the formation of di-fructose anhydride compounds. The immobilized enzyme retained about 60% of its initial activity after being used for 20 cycles.     

Mass transfer studies on the reduction of Cr(VI) using calcium alginate immobilized Bacillus sp. in packed bed reactor

This study presents the external mass transfer effects on the reduction of hexavalent chromium (Cr(VI)) using calcium alginate immobilized Bacillus sp. in a re-circulated packed bed batch reactor (RPBR). The effect of flow rate on the reduction Cr(VI) was studied. Theoretically calculated rate constants for various flow rates were analyzed using external film diffusion models and compared with experimental values. The external mass transfer coefficients for the bioconversion of Cr(VI) were also investigated. The external mass transfer effect was correlated with a model of the type J_D = K Re⁻⁽¹⁻ⁿ⁾. The model was tested with various K values and the mass transfer correlation J_D = 5.7 Re^−0.70 was found to predict the experimental data accurately. The proposed model would be useful for the design of industrial reactor and scale up.     

Immobilization of laccase from the white rot fungus Coriolopsis polyzona and use of the immobilized biocatalyst for the continuous elimination of endocrine disrupting chemicals

Laccase from the white rot fungus strain Coriolopsis polyzona was immobilized covalently on the diatomaceous earth support Celite^® R-633 using different strategies. A first methodology involved the sequential activation of the support surface with γ-aminopropyltriethoxysilane followed by the reaction of the functionalized surface with glutaraldehyde (GLU) or glyoxal (GLY) and the immobilization of laccase on the activated surface. Another strategy tested the simultaneous internal cross-linking of the protein with GLU or GLY and the immobilization of the laccase on the silanized surface. Finally, these two strategies were modified to test the impact of the concomitant addition of bovine serum albumin (BSA) as a stabilizing agent during the immobilization steps. The highest laccase activity and the greatest degree of activity recovery (tested using 2,2′-azino-bis-(3-ethylbenzthiazoline-6-sulfonic acid) (ABTS) as the substrate) were achieved by the sequential immobilization procedure using GLU as the cross-linking agent. The solid catalysts featuring internal cross-linking of the protein showed significantly higher stability against several denaturants. The Michaelis–Menten kinetic parameters with respect to ABTS revealed a higher affinity for this substrate in the case of the sequential procedure compared to the simultaneous approach. The biocatalyst formed using GLU in the sequential procedure was applied in a packed bed reactor for the continuous treatment of 5 mg l⁻¹ solutions of the endocrine disrupting chemicals (EDCs) nonylphenol (NP), bisphenol A (BPA) and triclosan (TCS) through repeated batch treatments. All of these EDCs could be eliminated at a contact time of less than 200 min by using, respectively, 3.75 units (U) of laccase activity for BPA and TCS and 1.88 U for NP. These performances of elimination were maintained over five consecutive treatment cycles using the same biocatalyst. This system could also remove these EDCs from 100 mg l⁻¹ solutions. The Michaelis–Menten kinetic parameters with respect to these chemicals showed a decreasing affinity of the solid biocatalyst for NP, TCS and BPA in that order.     

Maximizing the productivity of catalytic biofilms on solid supports in membrane aerated reactors

A new solid support membrane aerated biofilm reactor was designed for the synthesis of enantiopure (S)‐styrene oxide utilizing Pseudomonas sp. strain VLB120ΔC growing in a biofilm as biocatalyst. In analogy to traditional packed bed systems, maximizing the volumetric oxygen mass transfer capability (k_La) was identified as the most critical issue enabling a consistent productivity, as this parameter was shown to directly influence biofilm growth and biotransformation performance. A microporous ceramic unit was identified as an ideal microenvironment for biofilm growth and for efficient oxygen transfer. A uniform and dense biofilm developed on this matrix. Due to this dual function, the reactor configuration could be significantly simplified by eliminating additional packing materials, as used in traditional packed bed reactors. Up to now, a maximum productivity of 28 g L day^?1 was achieved by integrating an in situ substrate feed and an in situ product recovery technique based on a silicone membrane. The system was stable for more than 30 days before it was actively terminated. Biotechnol. Bioeng. 2010;106: 516–527. © 2010 Wiley Periodicals, Inc.     

A New Way to Investigate Living Flagellated/Ciliated Cells in the Light Microscope: Immobilization of Cells in Agarose

A method for cell immobilization of living flagellated/ciliated cells in agarose has been developed that allows single cells to be viewed for prolonged periods of time using high resolution light microscopy. Embedding in ultralow gelling, soft agarose preserves cellular functions of various flagellated/ciliated protists including delicate species, marine dinoflagellates, cryptomonads, contractile ciliates, etc. for days. Cell division, morphogenesis of cell organelles and intracellular movements can thus be studied for the first time in great detail. The method may also be useful for the isolation of flagellated/ciliated protists from nature and for the establishment of axenic clonal cultures in a single step.     

Use of computational fluid dynamics as a tool for establishing process design space for mixing in a bioreactor

The concept of "design space" plays an integral part in implementation of quality by design for pharmaceutical products. ICH Q8 defines design space as "the multidimensional combination and interaction of input variables (e.g., material attributes) and process parameters that have been demonstrated to provide assurance of quality. Working within the design space is not considered as a change. Movement out of the design space is considered to be a change and would normally initiate a regulatory post-approval change process. Design space is proposed by the applicant and is subject to regulatory assessment and approval." Computational fluid dynamics (CFD) is increasingly being used as a tool for modeling of hydrodynamics and mass transfer. In this study, a laboratory-scale aerated bioreactor is modeled using CFD. Eulerian-Eulerian multiphase model is used along with dispersed k-ε turbulent model. Population balance model is incorporated to account for bubble breakage and coalescence. Multiple reference frame model is used for the rotating region. We demonstrate the usefulness of CFD modeling for evaluating the effects of typical process parameters like impeller speed, gas flow rate, and liquid height on the mass transfer coefficient (k(L)a). Design of experiments is utilized to establish a design space for the above mentioned parameters for a given permissible range of k(L)a.     

Mass-transfer limitations for immobilized enzyme-catalyzed kinetic resolution of racemate in a fixed-bed reactor

A mathematical model has been developed for immobilized enzyme-catalyzed kinetic resolution of racemate in a fixed-bed reactor in which the enzyme-catalyzed reaction (the irreversible uni-uni competitive Michaelis-Menten kinetics is chosen as an example) was coupled with intraparticle diffusion, external mass transfer, and axial dispersion. The effects of mass-transfer limitations, competitive inhibition of substrates, deactivation on the enzyme effective enantioselectivity, and the optical purity and yield of the desired product are examined quantitatively over a wide range of parameters using the orthogonal collocation method. For a first-order reaction, an analytical solution is derived from the mathematical model for slab-, cylindrical-, and spherical-enzyme supports. Based on the analytical solution for the steady-state resolution process, a new concise formulation is presented to predict quantitatively the mass-transfer limitations on enzyme effective enantioselectivity and optical purity and yield of the desired product for a continuous steady-state kinetic resolution process in a fixed-bed reactor.     

Perfusion bioreactors for the production of recombinant proteins in insect cells

Conclusion High density perfusion culture of insect cells for the production of recombinant proteins has proved to be an attractive alternative to batch and fed-batch processes. A comparison of the different production processes is summarized in Table 3. Internal membrane perfusion has a limited scale-up potential but appears to the method of choice in smaller lab-scale production systems. External membrane perfusion results in increased shear stress generated by pumping of cells and passing through microfiltration modules at high velocity. However, using optimized perfusion strategies this shear stress can be minimized such that it is tolerated by the cells. In these cases, perfusion culture has proven to be superior to batch production with respect to product yields and cell specific productivity. Although insect cells could be successfully cultivated by immobilization and perfusion in stationary bed bioreactors, this method has not yet been used in continuous processes. In fluidized bed bioreactors with continuous medium exchange cells showed reduced growth and protein production rates.For the cultivation of insect cells in batch and fedbatch processes numerous efforts have been made to optimize the culture medium in order to allow growth and production at higher cell densities. These improved media could be used in combination with a perfusion process, thus allowing substantially increased cell densities without raising the medium exchange rate. However, sufficient oxygen supply has to be guaranteed during fermentation in order to ensure optimal productivity.     

Evidence for the importance of OxPAPC interaction with cysteines in regulating endothelial cell function

Oxidation products of 1-palmitoyl-2-arachidonoyl-sn-glycerol-3-phosphatidylcholine (PAPC), referred to as OxPAPC, and an active component, 1-palmitoyl-2-(5,6-epoxyisoprostane E₂)-sn-glycero-3-phosphatidylcholine (PEIPC), accumulate in atherosclerotic lesions and regulate over 1,000 genes in human aortic endothelial cells (HAEC). We previously demonstrated that OxPNB, a biotinylated analog of OxPAPC, covalently binds to a number of proteins in HAEC. The goal of these studies was to gain insight into the binding mechanism and determine whether binding regulates activity. In whole cells, N-acetylcysteine inhibited gene regulation by OxPAPC, and blocking cell cysteines with N-ethylmaleimide strongly inhibited the binding of OxPNB to HAEC proteins. Using MS, we demonstrate that most of the binding of OxPAPC to cysteine is mediated by PEIPC. We also show that OxPNB and PEIPE-NB, the analog of PEIPC, bound to a model protein, H-Ras, at cysteines previously shown to regulate activity in response to 15-deoxy-Δ12,14-prostaglandin J2 (15dPGJ₂). This binding was observed with recombinant protein and in cells overexpressing H-Ras. OxPAPC and PEIPC compete with OxPNB for binding to H-Ras. 15dPGJ₂ and OxPAPC increased H-Ras activity at comparable concentrations. Using microarray analysis, we demonstrate a considerable overlap of gene regulation by OxPAPC, PEIPC, and 15dPGJ₂ in HAEC, suggesting that some effects attributed to 15dPGJ₂ may also be regulated by PEIPC because both molecules accumulate in inflammatory sites. Overall, we provide evidence for the importance of OxPAPC-cysteine interactions in regulating HAEC function.     

生物膜型污水脱氮系统中膜结构及微生物生态研究进展

生物膜法污水脱氮系统主要利用生物膜中脱氮功能微生物的代谢活动去除氮素,从而达到净化水质的目的,研究脱氮生物膜的微观结构和微生物生态是揭示生物膜脱氮机理从而提高脱氮效率的重要途径.本文综述了生物膜型污水脱氮系统类型、生物膜微观结构特征及其影响因素、生物膜型污水脱氮系统内氮素传质过程、脱氮机理和生物膜数学模型等方面的研究进展.另外,本文介绍了生物膜型污水脱氮系统内生物膜脱氮功能微生物分布特征,不同生物膜脱氮系统、底物、运行条件和时间对功能微生物群落影响,及新型脱氮功能微生物等方面的研究进展,为生物膜脱氮技术的深入研究提供参考.     

Potential for use of a cyanobacterium Synechocystis sp. immobilized in poly(vinylalcohol): Application to the detection of pollutants

A cyanobacterium, Synechocystis sp. PCC 6803, was immobilized by entrapment in poly(vinylalcohol) bearing styrylpyridinium groups. Its properties in a single-compartment micro-photoelectrochemical cell using platinum electrodes in potentiosatic mode were compared with the native material. The operational activity was measured in the presence of an electrolytic solution containing 20 mM sodium phosphate, 0.15 mM NaCl and 1 mM MgCl₂. The best conditions of use are pH 7.0, 38 °C and a 2,5-dichlorobenzoquinone concentration equal to 350 M with native cyanobacteria or pH 6.5, 25 °C and 500 M 2,5-dichlorobenzoquinone after entrapment. Using this procedure, the photocurrent could be inhibited by pollutants such as Diuron or HgCl₂. After entrapment, the detection limits (corresponding to a 10% inhibition) were respectively 0.5 M and 50 M for Diuron and HgCl₂ after five minutes of incubation. A permeabilization technique was used to increase sensitivity of the procedure to the detection of HgCl₂ (25% inhibition with 50 M after five minutes of incubation).     

Mathematical analysis of solid-liquid mass transfer in a batch reactor for the enzymatic transformation of testosterone to 4AD

A previous mathematical analysis of mass transfer in a two-phase (solid-liquid) batch reactor for enzymatic transformation of testosterone to 4AD (Pereira et al., 1987) is extended to incorporate the effect of convective mixing. The results of the analysis showed that for a given enzyme loading, the mass transfer resistance in the solid (a function of the bead size) and the intensity of convective mixing (as embodied in the mass transfer coefficient) are two parameters that can be varied such that the overall mass transfer rate from the solid to the liquid phase ensures optimal reactor performance.     

用双向电泳和质谱技术检测NGX6转染后人鼻咽癌细胞表达差异的蛋白质(英)

NGX6是克隆的鼻咽癌相关基因,它的功能与作用机制目前尚不十分清楚.通过脂质体转染把NGX6导入鼻咽癌细胞株中,采用双向凝胶电泳分离细胞内所有蛋白质,通过软件分析,找到与未处理细胞表达差异的蛋白质,通过质谱分析和生物信息学资料处理.鉴定出七种表达上调的蛋白质,其中包括Fas蛋白,锌指蛋白（ZNF）,主要组织相容性抗原Ⅱ（MHCⅡ）等.Fas蛋白参与细胞凋亡的信号传导途径,它的上调可以促进细胞凋亡;ZNF蛋白参与基因的转录调控,它的上调也可影响细胞异常增殖的信号传导通路;MHCⅡ可以促进机体对肿瘤细胞的免疫应答.这些结果说明NGX6可能通过多种途径抑制鼻咽癌细胞的生长,为研究NGX6的作用机制提供了很好的实验资料,对鼻咽癌的基因治疗奠定了一定的研究基础,也为研究其他基因的作用机制提供了新思路.     

Coupling of the Human Y2 Receptor for Neuropeptide Y and Peptide YY to Guanine Nucleotide Inhibitory Proteins in Permeabilized SMS-KAN Cells

Abstract: Using guanine nucleotides, pertussis toxin, and specific antisera against the COOH-terminals of the α-subunits of G_i1/2, G_i3, and G_o, the binding and biological response of the Y2 receptor (Y2R) for peptide YY (PYY) was probed in SMS-KAN neuroblastoma cells. The specific binding of radiolabeled PYY exhibited a single apparent dissociation constant, K _D = 76 p M for intact cells and K _D = 906 p M for permeabilized cells. However, other data suggested existence of multiple receptor affinity states. A shift in K _D and a decrease in apparent number of binding sites ( B _max) was observed in permeabilized cells when incubated with guanine nucleotides. By contrast, in membrane preparations guanine nucleotides induced only a decrease in B _max. In intact cells, agonist exposure inhibited the intracellular accumulation of forskolin-stimulated cyclic AMP by 80% (IC₅₀ = 420 n M ) compared with 94% inhibition (IC₅₀ = 380 n M ) in permeabilized cells. In permeabilized cells, preincubation with antisera against α_i1/2 and α_i3 blocked the functional response of PYY, with anti-α_i3 being the most potent; whereas anti-α_o failed to affect the cyclic AMP levels. These results suggest that permeabilized SMS-KAN cells serve as a good model system for analysis of Y2R binding kinetics and functional response and that the Y2R interacts directly with several different G_is (but not G_o).