血红素加氧酶系的共固定化及部分性质研究

为了检测血红素加氧酶系分子间的相互作用和共固定化酶系的反应动力学,利用２′,５′－ＡＤＰ－Ｓｅｐｈａｒｏｓｅ４Ｂ柱对血红素加氧酶、ＮＡＤＰＨ－细胞色素ｃ还原酶和胆绿素还原酶进行非膜重组,再以纤维素为载体,用重氮化法固定此重组的酶复合物和共固定非重组的３种酶,发现固定化的重组酶系比非重组酶系能更好地发挥协同作用,在室温条件下可催化血红素一步合成胆红素．共固定化酶的最适ｐＨ为７．２,最适温度为３８℃,Ｋｍ值为０．９３μｍｏｌ／Ｌ．巯基试剂和金属卟淋对固定化酶有抑制作用,共固定化酶比游离酶系稳定性提高,３８℃下的操作半寿期可延长至４２０ｈ,在０～４℃保存两个月其酶活力无明显变化．     

Comparison between immobilized Kluyveromyces fragilis and Saccharomyces cerevisiae coimmobilized with beta-galactosidase, with respect to continuous ethanol production from concentrated whey permeate

Kluyveromyces fragilis immobilized in calcium alginate gel was compared to Saccharomyces cerevisiae coimmobilized with beta-galactosidase, for continuous ethanol production from whey permeate in packed-bed-type columns. Four different whey concentrations were studied, equivalent to 4.5, 10, 15, and 20% lactose, respectively. In all cases the coimmobilized preparation produced more ethanol than K. fragilis. The study went on for more than 5 weeks. K. fragilis showed a decline in activity after 20 days, while the coimmobilized preparation was stableduring the entrire investigation. Under experimental conditions theoretical yields of ethanol were obtained from 4.5 and 10% lactose substrates with the coimmobilized system. Using 15% lactose substrate, theoretical yields were only obtained when a galactose-adapted immobilized S. cerevisiae column was run in series with the coimmobilized column. Then a maximum of 71 g/L ethanol was produced with a productivity of 2.5 g/L h. The coimmobilized column alone gave a maximum ethanol concentration of 52 g/L with a productivity of 4.5 g/L h, whereas immobolized K. fragilis only produced 13 g/L ethanol with a productivity of 1.1 g/L h. It was not possible to obtain theoretical yields of ethanol from the highest substrate concentration.     

α淀粉酶与糖化酶的共固定化研究

以纤维素为载体用重氮化法同时固定了糖化酶和α淀粉酶,确定了共固定化的最适条件,研究了共固定化酶的性质,发现共固定化酶较固定化单酶能更好地发挥协同效应,能在较低温度下将淀粉一步水解为葡萄糖。共固定化酶在３０℃下的操作半寿期可达９２０小时。     

Oxygen supply to immobilized cells: 2. Studies on a coimmobilized algae—bacteria preparation with in situ oxygen generation

A coimmobilized mixed culture of algae, Chlorella pyrenoidosa, and bacteria, Gluconobacter oxydans, has been studied. The conversion of glycerol to dihydroxyacetone(1,3-dihydroxy-2-propanone), catalysed by the bacteria, was used to indicate the oxygen supply in the immobilized preparation. The oxygen produced by the algae in the coimmobilized preparation was used by the bacteria more effectively than when the cells were immobilized separately and mixed within the reactor. A preparation consisting of only bacteria and no algae was much less effective. The coimmobilized preparation was used in the continuous production of dihydroxyacetone for six days without any significant loss of activity.     

Use of coimmobilized biological systems to degrade toxic organic compounds

The concept of coimmobilizing cell mass (and/or enzyme) and adsorbent in a hydrogel matrix for biodegradation of toxic organic chemicals was introduced. Under defined experimental conditions, the coimmobilized system using activated carbon and Phanerochaete chrysosporium was compared with nonimmobilized systems for the degradation of pentachlorophenol (PCP). It was demonstrated that the coimmobilized system degraded PCP more effectively than the nonimmobilized system. A solid substrate included in the coimmobilized system could support the biodegradation. Isolation of the degrading agents from a model interrupting microorganism by the coimmobilized capsule membrane reduced the interference on the biodegradation. In simulated contaminated soil extract and sand, the coimmobilized system also exhibited higher degradative ability and stability than the nonimmobilized systems.     

Effective Bead Preparation of Coimmobilized Methanogenic and Methanotrophic Bacteria for Tetrachloroethene Degradation

Three types of coimmobilized methanogenic and methanotrophic bacterial beads – Ca-alginate, Ba-alginate, and Ca-alginate chitosan – were used for tetrachloroethene (PCE) degradation. For the purpose of effective preparation of coimmobilized bacterial beads, the diameter and broken-loading of beads were measured. The activity tests to find the optimal bacteria concentration in the bead were performed. It was found that Ba-alginate beads had superiority in bacterial growth and the degree of strength of beads from the diameter and broken-loading tests. Also, it was shown that it is most effective to add 200 mL of methanogens into 500 mL of 2% alginate solution and 20 mL of methanotrophs into 500 mL to 2% alginate solution. When methanogens and methanotrophs were applied with the Ba-alginate bead in the actual dechlorination of PCE, the biological PCE dechlorination rate was 92%, and there was highly effective degradation of PCE based on the coimmobilized bead. Additionally, relation to the diameter (X) and broken-loading (Y) of the Ba-alginate bead was derived following equation, Y = 438.02 exp(–1.4815 X).     

An enzyme coimmobilized with a microorganism: the conversion of cellobiose to ethanol using beta-glucosidase and Saccharomyces cerevisiae in calcium alginate gels

The efficiency of beta-glucosidase and Saccharomyces cerevisiae in directly converting cellobiose to ethanol was studied for various combinations of the two catalytic species, both free and immobilized, in order to elucidate the advantages of using a coimmobilized system. The coimmobilized preparation was superior to a combination of separately immobilized biocatalysts. However, in this preparation, one-half the enzyme activity was lost within a week when incubated at the operational temperature in the absence of substrate. In continuous experiments, an 80% conversion of cellobiose to ethanol was obtained using the coimmobilized preparation, compared to 40% using separately immobilized biocatalysts when applying a dilution rate of 0.1 h(-1) in a packedbed reactor. The immobilized biocatalysts showed no decline in productivity during two weeks of continuous operation.     

A two‐enzyme immobilization approach using carbon nanotubes/silica as support

Multiple enzyme mixtures are attractive for the production of many compounds at an industrial level. We report a practical and novel approach for coimmobilization of two enzymes. The system consists of a silica microsphere core coated with two layers of individually immobilized enzymes. The model enzymes α‐amylase (AA) and glucoamylase (GluA) were individually immobilized on carbon nanotubes (CNTs). A CNT‐GluA layer was formed by adsorbing CNT‐GluA onto silica microsphere. A sol‐gel layer with entrapped CNT‐AA was then formed outside the CNT‐GluA/silica microsphere conjugate. The coimmobilized α‐amylase and glucoamylase exhibited 95.1% of the activity of the mixture of free α‐amylase and glucoamylase. The consecutive use exhibited a good stability of the coimmobilized enzymes. The developed approach demonstrates advantages, including controlling the ratio of coimmobilized enzymes in an easy way, facilitating diffusion of small molecules in and out of the matrix, and preventing the leaching of enzymes. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:42–47, 2015     

Enzymatic transformation of cephalosporin C to 7-amino-cephalosporanic acid. Part II: Single-step procedure using a coimmobilized enzyme system

The enzymatic transformation of cephalosporin C to 7-amino-cephalosporanic acid (7-ACA) using coimmobilized -aminoacid oxidase (DAAO) and 7-β-(4-carboxybutanamido)cephalosporanic acid acylase (Gl-7-ACA acylase) is reported. The results from the coimmobilization of the two enzymes on different carriers and at different ratios of enzyme activities are described. When an inhibitor of catalase activity, such as NaN₃ or H₂O₂, is present, the conversion rate to 7-ACA is higher, but more by-products are obtained. An optimum ratio of 60:1 between the enzymatic activities of DAAO and Gl-7-ACA acylase in the coimmobilized sample at 0.21 Ug⁻¹ Gl-7-ACA acylase activity was determined. The results of using coimmobilized enzymes and of using a mixture of separately immobilized enzymes in the same process are compared.     

Kinetic modeling of a multiple immobilized enzyme system. I. Development and testing of the model

A kinetic model for the reaction sequence catalyzed by coimmobilized invertase and glucose oxidase with a sucrose substrate in a tubular reactor has been developed. The computerized mathematical model employs and orthogonal collection technique for solving oxidase were coimmobilized in poly(2-hydroxyethlmethacrylate) gels and used in a continuous flow packed-bed tubular reactor system. In addition to describing the development of the kinetic model, this article compares experimentally determined reactor effluent concentrations for various sucrose feed solutions to those predicted by the model. Variations between experimental and predicted reactor effluent concentrations were found to be on the micromolar level for sucrose feed concentrations as low as 1.38mM.     

Simultaneous saccharification and alcohol fermentation of unheated starch by free,immobilized and coimmobilized systems of glucoamylase and Saccharomyces cerevisiae

For the simultaneous saccharification and alcohol fermentation (SSF) of corn, cassava and naked barley requiring no heat treatment, the use of freely syuspended glucoamylase-cell, cell immobilized and glucoamylase-cell coimmobilized systems in Ca-alginate was investigated.In these systems, 0.2% glucoamylase was used for both the free glucoamylase-cell and cell immobilized systems, whereas 1.0% of the enzyme was used for the glucoamylase cell coimmobilized system.The SSF of corn, cassava and naked barley was successfully carried out as follows; group A with heat treatment and group B without heat treatment using the glucoamylase-cell suspende system. The conversion yield (Y_p/s0) in the cell immobilized system was increased by the heat treatment of corn and cassava but not of naked barley. The conversion yield was remarkably increased using the coimmobilized system corn and cassava, whereas naked barley gave the same yield as in the free glucoamylase-cell suspended system.     

Ethanol production from starch by a coimmobilized mixed culture system of Aspergillus awamori and Zymomonas mobilis

The production of ethanol from starch by a coimmobilized mixed culture system of aerobic and anaerobic microorganisms in Ca-alginate gel beads was investigated. The mold Aspergillus awamori was used as an aerobic amylolytic microorganism and an anaerobic bacterium, Zymomonas mobilis, as an ethanol producer. By controlling the mixing ratio of the microorganisms in the inoculum size, a desirable coimmobilized mixed culture system, in which the aerobic mycelia grew on and near the oxygen-rich surface of the gel beads while the anaerobic bacterial cells mainly grew in the oxygen-deficient central part of the gel beads, was naturally established under the aerobic culture conditions, and ethanol could be directly produced from starch by the system. The ethanol productivity by the system in flask culture was particularly affected by the shear stress (dependent on the shaking speed) which controlled the mycelial growth on the surface of the gel beads. Under optimum culture conditions in the flask culture, the glucose produced was instantly consumed, and was not observed in the culture broth; the final concentration of ethanol produced from 100 g/L starch was 25 g/L and the yield coefficient for ethanol, Y(pls), was 0.38. The ethanol productivity by the coimmobilized mixed culture system was compared with those by other various culture systems and the advantages of the system were clarified.     

Coimmobilization of L-asparaginase and glutamate dehydrogenase onto highly activated supports

In the present research work, production of coimmobilized derivatives of L-asparaginase and glutamate dehydrogenase was attempted. Comparison of immobilization of each enzyme independently with coimmobilization of the two enzymes unfolded important advantages of the latter, namely a decrease in the induction period (time before the maximum reaction rate is virtually achieved) and an increase in the maximum reaction rate. The effectiveness of the independent enzyme derivatives was low; however, it was enhanced by three-fold when the enzymes were coimmobilized onto the same agarose-glutaraldehyde support. Each supporting agarose bead may in fact be viewed as a nano-reactor with in situ reaction and separation (i.e. elimination of the ammonia formed), with the nanoenvironment surrounding each enzyme molecule being essentially devoid of steric hindrance.     

Enzyme immobilization on a low-cost magnetic support: kinetic studies on immobilized and coimmobilized glucose oxidase and glucoamylase.

Glucose oxidase (GOx) and glucoamylase (GA) were immobilized and coimmobilized through their carbohydrate moieties onto polyethyleneimine-coated magnetite crosslinked with glutaraldehyde and derivatized with adipic dihydrazide. The carbohydrates were oxidized with sodium periodate, and at optimal concentration, their Vm increased up to 18% for GOx and up to 16% for GA. After immobilization, a remaining activity as high as 88% and 70% for GA with maltose and maltodextrin respectively as substrates was obtained, independently of the particle loading. On the contrary, the remaining activity of GOx strongly decreased at high particle loading. Nevertheless, half of its initial activity was recovered at low loading and was not significantly affected when GA was coimmobilized by saturating the reactive groups left on the particle. The Vm of both immobilized enzymes was improved by crosslinking their carbohydrates with adipic dihydrazide, a treatment which allows further coimmobilization of the other enzyme on a second layer.     

Ethanol production from starch by a coimmobilized mixed culture system of Aspergillus awamori and Saccharomyces cerevisiae

The development of a coimmobilized mixed culture sys tem of aerobic and facultative anaerobic microorganisms in Ca-alginate gel beads and the production of useful metabolites by the system were investigated. A coimmobilized mixed culture system of Aspergillus awamori (obligate aerobe) and Saccharomyces cerevisiae (facultative anaerobe) in Ca-alginate gel beads was used as a model system, and ethanol production from starch by the system was used as a model production. Mold Asp. awamori is an amylolytic microorganism while yeast S. cerevisiae is an ethanol producer. The two microorganisms grew competitively in the oxygen-rich surface area of the gel beads because they had similar oxygen demands in aerobic culture conditions. Neither microorganism exhibited "habitat segregation" in the gel beads and leaked yeast cells grew aerobically without ethanol production in the broth. Ethanol productivity was low under these conditions.A more desirable coimmobilized mixed culture system of Asp. awamori and S. cerevisiae was established by adding Vantocil IB (a biocidal compound) to the production medium. The antimicrobial activity of Vantocil IB was more effective with S. cerevisiae than with Asp. awamori, so that a dense mycelial layer of Asp. awamori formed in the surface of the gel beads While S. cerevisiae grew densely in the more inner areas of the gel beads. Also, yeast cell leakace was repressed and ethanol productivity was improved. The system with Vantocil IB produced ethanol of 4.5 and 12.3 g/L from 16 and 40 g/L starch, respectively. A continuous culture using this system with Vantocil IB was also carried out, and a stable steady state could be maintained for six days without leakage of yeast cells and contamination. The selection of a factor suitable for producing "habitat segregation" enabled the development of a coimmobilized mixed culture system of an aerobe and a facultative anaerobe. In this study, total habitat segregation was used to denote a tendency to exhibit denser growth in different parts of one gel bead.     

Effect of adsorbents on degradation of toxic organic compounds by coimmobilized systems

The use of coimmobilized systems for treatment of toxic organic compounds has been proposed. The proposed approach combines the use of adsorbents and laboratory identified microorganisms immobilized in a protective permeable barrier to achieve a greater degree of control over the remediation process. This study was launched to understand the effect of adsorbents and changes in adsorption on the degradation of toxic compounds by coimmobilized systems. The specific case studied involved the degradation of pentachlorophenol (PCP) by Arthrobacter (ATCC 33790) coimmobilized with powdered activated carbon within calcium alginate capsules.The design parameters studied included adsorbent content and type as well as the effect of solution pH and surfactant concentration on adsorption and biodegradation. It was found that the equilibrium adsorption behavior of PCP was strongly influenced by solution pH and surfactant concentration. A mathematical model was developed that combined the physical processes of mass transfer and adsorption with biological degradation of PCP. The model was used to predict the effect of various parameters on the degradation of PCP. Based on model predictions, the degradation of PCP. Based on model predictions, the degradation of PCP was strongly dependent on variations in adsorbent capacity and affinity for this contaminant.     

Coimmobilized whole cells of Pseudomonas reptilivora and Micrococcus glutamicus in calcium alginate gel for the production of L-glutamic acid

A novel method of coimmobilized whole cells of Pseudomonas reptilivora and Micrococcus glutamicus, entrapped in calcium alginate beads have been used for the production of L-glutamic acid in a single stage fermentation process, using selected production medium enriched with glucose as substrate. The results obtained were compared with the L-glutamic acid production by free cells of Micrococcus glutamicus and by mixed culture of Pseudomonas reptilivora and Micrococcus glutamicus. The yield of glutamic acid obtained with mixed culture is relatively more than that the yield obtained with Micrococcus glutamicus alone. The properties of coimmobilized whole cells of Pseudomonas reptilivora and Micrococcus glutamicus in calcium alginate gel matrix have been investigated thoroughly and compared with those of free cells under most suitable conditions of fermentation.     

Coimmobilization of Nitrosomonas europaea and Paracoccus denitrificans cells using polyelectrolyte complex-stabilized calcium alginate gel

Calcium alginate gel (CAG) that withstands phosphate ions in the medium was prepared by reinforcing a network structure of the gel with a polyelectrolyte complex (PEC) consisting of potassium poly(vinyl alcohol) sulfate and trimethylammonium glycol chitosan iodide. The PEC-stabilized CAG beads were used as a supporting matrix for the coimmobilization of Nitrosomonas europaea ATCC 25978 cells and Paracoccus denitrificans IFO 12442 cells. The coimmobilized cells were aerobically cultured on a medium containing 3 mM of phosphate ions, using (NH₄)₂SO₄ as a substrate and ethanol as a carbon source. Ammonia was consumed without forming nitrite, indicating the concurrence of nitrification and denitrification in the same system. No breakage of the gel beads was observed during the cultivation. Repeated aerobic cultivation using a column packed with beads of coimmobilized cells had stable initial activity for at least one month.     

Continuous production of glutathione using immobilized microbial cells containing ATP generating system

Acetate kinase reaction in Escherichia coli cells and glycolytic pathway in Saccharomyces cerevisiae cells were utilized as ATP generation systems for glutathione synthetic processes. These two ATP generation systems were well coupled with glutathione synthetase reactions and glutathione was produced by coimmobilized E. coli cells with dextran-bound ATP or by immobilized S. cerevisiae cells. The glycolytic pathway in S. cerevisiae cells was further utilized for the biosynthetic processes of other useful compounds.     

Development of a multienzyme reactor for dopamine synthesis: II. Reactor engineering and simulation

Aspects of reaction engineering associated with multienzyme reactions have been studied in a system where dopamine is produced from catechol, pyruvate and ammonium by sequential enzymatic reactions catalyzed by tyrosine phenol lyase (TPL) and tyrosine decarboxylase (TDC). Microbial cells containing TPL activity (Erwinia herbicola) and TDC activity (Streptococcus faecalis) were coimmobilized in glutaraldehyde cross-linked porcine gelatin beads with a mean diameter of 2.8 mm for use in the reactions. Measurement of the transport properties in the beads indicate that the gelatin matrix does not significantly increase the diffusion resistance and that dopamine partitions into the matrix (K = 2). A packed-bed reactor containing the coimmobilized cell beads successfully produced dopamine, although with a low conversion. Using computer simultaneous it is shown that separate, sequential TPL and TDC, rather than simultaneous, reactions, would require smaller reactors overall for the same conversion. (c) 1992 John Wiley & Sons, Inc.