Biodegradation of coumaphos, chlorferon, and diethylthiophosphate using bacteria immobilized in Ca-alginate gel beads

Calcium-alginate immobilized cell systems were developed for the detoxification and biodegradation of coumaphos, an organophosphate insecticide, and its hydrolysis products, chlorferon and diethlythiophosphate (DETP). Optimum bead loadings for bioreactor operation were found to be 200 g-beads/L for chlorferon degradation and 300 g-beads/L for DETP degradation. Using waste cattle dip (UCD) solution as substrate, the degradation rate for an immobilized consortium of chlorferon-degrading bacteria was five times greater than that for freely suspended cells, and hydrolysis of coumaphos by immobilized OPH(+)Escherichia coli was 2.5 times greater. The enhanced degradation of immobilized cells was due primarily to protection of the cells from inhibitory substances present in the UCD solution. In addition, physiological changes of the cells caused by Ca-alginate immobilization may have contributed to increased reaction rates. Degradation rates for repeated operations increased for successive batches indicating that cells became better adapted to the reaction conditions over time.     

Immobilization of liver microsomal cytochrome P-450

Rabbit liver microsomal cytochrome P-450 was immobilized by entrapment in calcium alginate gel. Aminopyrine demethylation experiments showed that the immobilized enzyme system is highly active and exhibits an unimpaired functional stability as compared with crude microsomes. The alginate entrapped microsomes were employed in a fixed bed recirculation reactor, where aminopyrine was continuously demethylated. Such model enzyme reactor can be a useful tool for studying extracorporeal drug detoxification or preparative substrate conversion with microsomal enzyme systems.     

Enhanced-rate biodegradation of organophosphate neurotoxins by immobilized nongrowing bacteria

Pesticide wastes generated from livestock dipping operations containing the organophosphate (OP) insecticide coumaphos (CP) are well suited for disposal by biodegradation since they are highly concentrated (approximately 1 g/L), generally contained, and lack additional toxic components. In this study, a significantly enhanced efficiency of degrading CP in cattle dip waste (CDW) is reported using a dense, nongrowing cell population that functions without the addition of nutrients required for growing cell cultures. A recombinant strain of Escherichia coli containing the opd gene for organophosphate hydrolase (OPH), which is capable of active hydrolysis of OP neurotoxins including CP, was cultivated in a rich medium containing all essential nutrients. Cells were harvested and utilized in lab scale experiments in the form of either freely suspended cells or cells immobilized within a macroporous gel matrix, poly(vinyl alcohol) (PVA) cryogel. Significantly higher degradation rates were achieved with either suspended or immobilized OPH(+) cells compared to rates with the microbial consortium naturally present in CDW. Of the two nongrowing cell systems, the detoxification rate with immobilized cells was approximately twice that of freely suspended cells, and kinetic studies demonstrated that a higher maximum reaction rate was achieved with the immobilized cell system. A comparative study using both the CDW and pure CP substrates with free cells indicated that the CDW contained one or more factors that reduced the bioavailability of CP. The immobilized cells retained their activity over a 4-month period of use and storage, demonstrating both sustained catalytic activity and long-term mechanical stability.     

Applications of purification reactions for minimizing reaction-generated enzyme poisoniong

A mathematical model has been employed to examine the interplay of reaction and mass transfer in immobilized enzyme systems involving reaction-generated enzyme poisons. Deactivation rates can be significantly reduced in some cases by catalyzing a purification reaction in which the poison is transformed into an innocuous substance. This conclusion is illustrated experimentally for reaction-generated H₂O₂ in a continuous-flow stirred slurry reactor containing glucose oxidase immobilized on activated carbon.     

Properties of a reversible soluble-insoluble cellulase and its application to repeated hydrolysis of crystalline cellulose

Cellulase was covalently immobilized on an enteric coating polymer, Eudragit L, that is reversibly soluble and insoluble depending on the pH of the medium. The hydrolysis of solid cellulose with the immobilized enzyme can take advantage of the soluble property of the immobilized enzyme itself at the most reactive pH value; on the other hand, recovery of the enzyme can take advantage of the insoluble property of the enzyme at other pH values. It was experimentally confirmed that 100% of immobilized enzyme activity in solution can be recovered by precipitation and by dissolving it again by alternative change of pH. After a period of hydrolysis, immobilized enzyme and unreacted cellulose were precipitated together to remove the product-the soluble sugar solution-by changing pH. Following this, a new buffer solution was added to the precipitate to dissolve it and resume the reaction. This was repeated several times. The hydrolysis rate of this process increased significantly compared with that of a batch process. Utilization of the reversible soluble-insoluble carrier for immobilizing enzyme is promising, not only for cellulose-cellulase systems, but also for other heterogeneous reaction systems.     

Continuous production ofL-malic acid by immobilizedBrevibacterium ammoniagenes cells

Summary Continuous production ofL-malic acid from fumaric acid using immobilized microbial cells was investigated. Several microorganisms having fumarase activity were immobilized into a polyacrylamide gel lattice. Among the microorganisms tested, immobilizedBrevibacterium ammoniagenes IAM 1645 showed the highest enzyme activity, but produced an unwanted by-product, succinic acid. Conditions for suppression of this side reaction were investigated, and bile extract treatment of immobilized cells was found to be effective.The bile extract treatment of immobilized cells also resulted in a marked increase of reaction rate forL-malic acid formation.No difference was observed between the native enzyme and immobilized cells in optimal pH and temperature of the enzyme reaction.The effect of temperature on the reaction rate and the stability of fumarase activity of an immobilized cell column were investigated under conditions of continuous enzyme reaction. The decay of enzyme activity during continuous enzyme reaction was expressed by an exponential relationship. Half-life of the fumarase activity of the immobilized cell column at 37°C was calculated to be 52.5 days.Presented at the Annual Meeting of the Society of Fermentation Technology, Japan, Osaka, Japan, October 30, 1975.     

Immobilization of Escherichia coli cells containing aspartase activity with kappa-carrageenan. Enzymic properties and application for L-aspartic acid production.

Whole cells of Escherichia coli having high aspartase (L-asparate ammonialyase, EC 4.3.1.1) activity were immobilized by entrapping into a kappa-carrageenan gel. The obtained immobilized cells were treated with glutaraldehyde or with glutaraldehyde and hexamethylenediamine. The enzymic properties of three immobilized cell preparations were investigated, and compared with those of the soluble aspartate. The optimum pH of the aspartase reaction was 9.0 for the three immobilized cell preparations and 9.5 for the soluble enzyme. The optimum temperature for three immobilized cell preparations was 5--10 degrees C higher than that for the soluble enzyme. The apparent Km values of immobilized cell preparations were about five times higher than that of the soluble enzyme. The heat stability of intact cells was increased by immobilization. The operational stability of the immobilized cell columns was higher at pH 8.5 than at optimum pH of the aspartase reaction. From the column effluents, L-aspartic acid was obtained in a good yield.     

Comparison of methods for thermolysin-catalyzed peptide synthesis including a novel more active catalyst

This is a comparative study of the performance of thermolysin for enzymatic peptide synthesis by reversed hydrolysis in several different reaction systems. Z-Gln-Leu-NH(2) was synthesized in acetonitrile containing 5% water (with various catalyst preparation methods) as well as by the "solid-to-solid" and frozen aqueous methods. Reaction rates (values in nanomoles per minute per milligram) in acetonitrile depended significantly on the method of addition of enzyme: (a) direct suspension in the reaction mixture as freeze-dried powders gave 60 to 95; (b) addition as an aqueous solution, so that enzyme precipitates on mixing with acetonitrile, gave 230; (c) addition as an aqueous suspension gave a remarkable increase in reaction rates (up to 780); (d) immobilized enzymes (adsorbed at saturating loading on celite, silica, Amberlite XAD-7, or polypropylene, then dried by propanol rinsing) all gave <230. It is postulated that, starting with the enzyme already in the form of solid particles in aqueous buffer, there is a minimum chance of alteration of its optimal conformation during transfer to the organic medium. For solid-to-solid synthesis with 10% water content we found initial rates of 670 under optimized conditions. In frozen aqueous synthesis, rates were <10. Equilibrium yields were always around 60% in low water organic solvent, whereas they were found to >80% in the aqueous systems studied.     

Urokinase bound to fibrocollagenous tubes: an in vitro kinetic study

Urokinase (UK) has been immobilized to the inner surfaces of fibrocollagenous tubes (FCT) in an attempt to develop a fibrinolytic biomaterial which may be suitable for use as a small diameter vascular prosthesis. The enzyme was bound by adsorption followed by glutaraldehyde crosslinking. An in virto kinetic study of immobilized urokinase was conducted by employing the tubular material as a flow through reactor operated in a batch recycle mode in which the esterolysis of the model substrate, N-alpha-acetyl-L-lysine methyl ester (ALME), was monitored as a function of substrate concentration, recycle flow rate, and temperature. Results were compared with data from the soluble enzyme reaction, which was conducted in the presence and absence of 10% swine skin gelatin, in order to identify the specific effects of a collagenous microenvironment. Observed rates for the UK-FCT catalyzed reaction were observed to be dependent on recycle flow rates below 12 mL/min (Re = 107). Apparent Michaelis-Menten rate parameters were determined by a nonlinear search technique for two flow rates: one above the critical point for external diffusion effects (Re = 282) and one within the mass-transfer-limited region (Re = 71). When the latter data were corrected for external diffusion by applying the Graetz correlation for laminar flow in tubes to estimate themass transfer coefficient, the corrected K(m) of 6.45 +/- 0.38 mM agreed very closely with the diffusion free parameter (i.e. 6.13 +/- 0.63). Furthermore, this value was observed to be an order of magnitude higher than that of the soluble enzyme but approximately equal to the K(m) of the soluble enzyme in a 10% gelatin environment (8.13 +/- 1.53 mM). It is postulated that the difference in kinetic parameters between soluble and collagen immobilized UK is due to an inherent interaction between collagen and enzyme rather than to mass transfer effects. Such aninteraction is supported by the effects of collagen on thermal stability and energy of activation.     

Regeneration of NADH in a bioreactor using yeast cells immobilized in alginate fiber: I. Method and effect of reactor variables

Saccharomyces cerevisiae cells immobilized in a calcium alginate fiber reactor were used as a source of alcohol dehydrogenase for the NAD(+)-to-NADH reaction. The reaction was catalyzed by enzyme in cells on the surface of the fiber. Internal diffusional effects were present. The enzyme cell concentration was optimized by harvesting cells finally grown under anaerobic conditions. The results were expressed as an apparent reaction rate constant that was independent of NAD(+) and excess ethanol concentration, was slightly affected by flow rate above a minimum value, and increased with immobilized cell concentration in the fiber. The reaction was complete after 6 to 7 h under optimal conditions of 36 degrees C and 9.5 pH. The latter was 0.5 pH units above the free enzyme optimum, indicating that microenvironmental effects were in evidence. (c) 1993 John Wiley & Sons, Inc.     

Properties and repeated use of a reversibly soluble-insoluble yeast lytic enzyme

Summary A yeast lytic enzyme was covalently immobilized on an enteric coating polymer, Eudragit S, that is reversibly soluble and insoluble (S-IS) depending on the pH of the reaction medium. The yeast lytic enzyme immobilized on Eudragit S (Y-E) showed a sharp response of solubility to slight changes in pH without decrease in enzymatic activity. The specific activity per amount of enzyme protein of Y-E for dry yeast cells was about two-thirds that of the native enzyme. In both lysis reactions of dry and pressed baker's yeast cells, changing the pH of the reaction medium from 7.0 to 4.8 at an appropriate interval allows the insoluble Y-E and the reaction products (soluble protein for dry yeast cells and invertase and soluble protein for pressed baker's yeast cells) to be repeatedly separated. The reaction method using a reversible S-IS enzyme is a promising procedure for repeated use of the enzyme in a heterogeneous reaction system containing yeast cells as a substrate.     

Reverse micelles as life-mimicking systems

In this review, we attempt to demonstrate that reverse micelles are simple artificial systems that mimic many life systems from cell division to the creation of an enzyme catalytic mechanism. For a membranous enzyme like placental alkaline phosphatase, the kinetic properties observed in reverse micelles might represent those found under physiological conditions. The reverse micellar system, consisting of a positively charged surfactant, mimics a detoxification enzyme glutathione transferase. We propose a novel island-in-oil-lake reverse micellar model for the glutathione transferase that can account for almost all the catalytic properties of this enzyme. Reverse micelles may provide an excellent model system in investigating the reaction mechanism of other detoxification enzymes.     

固定化青霉素酰化酶在光-pH敏感可回用两水相中裂解青霉素G为6-APA

两水相体系在发展中存在的关键问题是相体系回收困难.由于生产成本及降低污染的原因, 用过的相体系需要回收和重复使用.用环境敏感型溶解可逆聚合物形成可回用两水相体系是当前是为可行的回收方法。本文在光敏感可回用高聚物PNBC与pH敏感型可回用高聚物PADB形成的两水相体系中进行固定化青霉素酰化酶的相转移催化青霉素G产生6-APA的反应。在这个两水相体系中,通过优化,在1% NaCl 存在下,６－ＡＰＡ的分配系数可达5.78。催化动力学显示,达平衡的时间近7h,反应最高得率约85.3%（pH 7.8, 20℃）。较相近条件下的单水相反应得率提高近20%。在反应过程中,通过底物及产物的分配系数检测,发现底物分配系数变化不大,而产物6-APA及苯乙酸的分配系数发生很大变化,从而引起产物的得率变化。在两水相中,底物及产物主要分配在上相,固定化酶分配在下相,底物青霉素G进入下相经酶催化产生的6-APA及苯乙酸又转入上相,从而解除了青霉素酰化酶催化反应的底物及产物抑制作用,达到提高产物得率的效果。此外,采用固定化酶较固定化细胞效率高,占用下相体积小,较游离酶稳定性高,且完全单侧分配在下相。因此,在两水相中进行固定化酶的催化反应具有明显的优越性。形成两水相的高聚物PNBC通过488 nm 的激光照射或经滤光的450nm 光源照射得到回收;pH敏感型成相聚合物PADB可通等电点 4.1沉淀可实现循环利用,高聚物的回收率在95%-98%之间,按此回收率计算,聚合物可使用60次以上。     

Modeling the performance of immobilized α-chymotrypsin catalyzed peptide synthesis in acetonitrile medium

A model was developed which describes simultaneous reaction and internal diffusion for kinetically controlled, immobilized α-chymotrypsin-catalyzed, oligopeptide synthesis in acetonitrile medium. The model combines the equations that describe the intrinsic kinetics of four different reactions and the physical characteristics of three different support materials, as determined experimentally, to predict the apparent initial activity and nucleophile selectivity of the immobilized biocatalyst. The model is able to predict reasonably well the experimentally observed initial rate and nucleophile selectivity vs. enzyme loading profiles. The reduction in observed initial rate with enzyme loading when fast reactions are carried out with α-chymotrypsin immobilized on celite, and the larger influence of mass transfer limitations on the initial reaction rates than on nucleophile selectivities are correctly predicted by the numerical calculations. The model is general in terms of its application to other systems — enzymes, reactions, support materials and/or kinetic schemes — as long as the intrinsic kinetics and the characteristics of the enzyme and support material are known.     

Glycolytic pathway as an ATP generation system and its application to the production of glutathione and NADP

Efficient ATP generation is required to produce glutathione and NADP. Hence, the generation of ATP was investigated using the glycolytic pathway of yeast. Saccharomyces cerevisiae cells immobilized using polyacrylamide gel generated ATP from adenosine, consuming glucose and converting it to ethanol and carbon dioxide. Under optimal conditions, the ATP-generating activity of immobilized yeast cells was 7.0 μmol h^?1 ml^?1 gel. A column packed with these immobilized yeast cells was used for continuous ATP generation. The half-life of the column was 19 days at a space velocity of (SV) 0.3 h^?1 at 30°C. The properties of glutathione- and NADP-producing reactions coupled with the ATP-generating reaction were investigated. Escherichia coli cells with glutathione synthesizing activity and Brevibacterium ammoniagenes cells with NAD kinase activity were immobilized in a polyacrylamide gel lattice. Under optimal conditions, the immobilized E. coli cells and immobilized B. ammoniagenes cells produced glutathione and NADP at the rates of 2.1 and 0.65 μmol h^?1 ml^?1 gel, respectively, adding ATP to the reaction mixture. In order to produce glutathione and NADP economically and efficiently, the glutathione- and NADP-producing reactions were finally coupled with the ATP-generating reaction catalysed by immobilized S. cerevisiae cells. To compare the productivities of glutathione and NADP, and to compare the efficiency of ATP utilization for the production of these two compounds, the two reactor systems, co-immobilized cell system and mixed immobilized cell system, were designed. As a result, these two compounds were also found to be produced by these two kinds of reactor systems. Using the data obtained, the feasibility and properties of ATP generation by immobilized yeast cells are discussed in terms of the production of glutathione and NADP.     

Production of acrylamide using immobilized cells of<Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> M33

The cellsof Rhodococcus rhodochrous M33, which produce a nitrile hydratase enzyme, were immobilized in acrylamide-based polymer gels. The optimum pH and temperature for the activity of nitrile hydratase in both the free and immobilized cells were 7.4 and 45°C, respectively, yet the optinum temperature for acrylamide production by the immobilized cells was 20°C. The nitrile hydratase of the immobilized cells was more stable with acrylamide than that of the free cells. Under optimal conditions, the final acrylamide concentration reached about 400 g/L with a conversion yield of almost 100% after 8 h of reaction when using 150 g/L of immobilized cells corresponding to a 1.91 g-dry cell weight/L. The enzyme activity of the immobilized cells rapidly decreased with repeated use. However, the quality of the acrylamide produced by the immobilized cells was much better than that produced by the free cells in terms of color, salt content, turbidity, and foam formation. The quality of the aqueous acrylamide solution obtained was found to be of commercial use without further purification.     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.     

固定化细胞生产L—苹果酸动力学及两种酶反应器的比较

研究了产氨短杆菌ＭＡ－２,黄色短杆菌ＭＡ－３的固定化细胞在富马酸铵转化体系中生成Ｌ－苹果酸的动力学参数,同时比较了固定化细胞在填充床及连续机械搅拌反应器中酶转化反应的差异。研究结果表明：当转化率小于４０％时,酶反应在两种反应器所需的停留时间相当。随着转化率的提高,填充床反应器较连续机械搅拌反应器所需的停留时间短且不会因剪切力使固定化颗粒受到损伤,因此,在富马酸铵体系中用固定化酶生产Ｌ－苹果酸采用填     

Kinetcs and decay of fumarase activity of immobilized Brevibacterium ammoniagenes cells for continuous production of L-malic acid

The kinetics of the reversible fumarase reaction of immobilized Brevibacterium ammoniagenes cells and the decay behavior of enzyme activity were investigated in a plug flow system. The time course of the reaction in the immobilized cell column was well explained by the time-conversion equation including the apparent kinetic constants of the immobilized cell enzyme. The decay rate of fumarase activity was faster in the upper sections of the column (inlet side of the substrate solution) compared with the lower sections when 1M sodium fumarate (pH 7.0) was continuously passed through the column at 37°C. It was shown that the decay rate of the fumarase activity in the immobilized cell column depends on the flow rate of the substrate solution. The effect of flow rate on the decay rate of enzyme activity was considered to be related to the rate of contamination of enzyme with poisonous substances derived from the substrate solution or to the rate of leakage of enzyme stabilizers and/or enzyme itself from the immobilized cells.     

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.