Effect of environmental growth conditions on plasmid stability, plasmid copy number, and catechol 2,3-dioxygenase activity in free and immobilized Escherichia coli cells

In order to better understand the high plasmid stability in immobilized recombinant E. coli cells, the effects of dilution rate on the pTG201 plasmid stability, the copy number, and the catechol 2,3-dioxygenase (encoded by XyIE gene) production were, at first, studied in free E. coli W3101 continuous cultures in minimal media. It was found that decreasing specific growth rate increased the plasmid copy number and the catechol 2,3-dioxygenase activity but the stability decreased. In continuous culture with immobilized cells, an increase was shown in plasmid copy number and catechol 2,3-dioxygenase activity probably due to the distribution of growth in the gel beads. Besides mechanical properties of gel beads which may allow limited cell divisions, the increase in plasmid copy number is involved in enhanced plasmid stability in immobilized cells. In the same way, an experiment conducted in LB medium dealing with competition between pTG201-free and pTG201-containing E. coli B cells was described. It was shown that the competition was not more pronounced in gel bead compared to a free system. The effects of nutritional limitations on pTG201 plasmid stability and catechol 2,3-dioxygenase activity during chemostat cultivations in free and immobilized E. coli B cells were also investigated. It was found that immobilization of cells increased the stability of pTG201 even under glucose, nitrogen, or phosphate limited cultures. However in the case of magnesium depleted culture, pTG201 was shown to be relatively instable and a decrease in viable cell number during the immobilized continuous culture was observed. By contrast to the free system, the catechol 2,3-dioxygenase activity increased in immobilized cells under all culture conditions used.     

Catechol 2,3-dioxygenase from the thermophilic, phenol-degrading Bacillus thermoleovorans strain A2 has unexpected low thermal stability

Catechol 2,3-dioxygenase from the thermophilic Bacillus thermoleovorans A2 was purified and characterized. The catechol 2,3-dioxygenase has a molecular mass of 135 000 Da and consists of four identical subunits of 34 700 Da. One iron per enzyme subunit was detected using atom absorption spectroscopy. Enzyme activity was not inhibited by EDTA, suggesting that the iron is tightly bound. Addition of hydrogen peroxide to the enzyme completely destroyed activity, indicating that the iron was in the divalent state. The isoelectric point of the enzyme was 4.8. The enzyme displayed optimal activity at pH 7.2 and 70°C. The half-life of the catechol 2,3-dioxygenase at the optimum temperature was 1.5 min under aerobic conditions and 10 min in a nitrogen atmosphere. This stability of the enzyme is comparable to the stability of the enzyme from the mesophilic Pseudomonas putida mt-2. The stability of the cloned enzyme in E. coli extracts was identical to the stability in wild-type extracts, suggesting that no stabilizing factors were present in Bacillus thermoleovorans A2 In whole cells the half-life of the enzyme at 70°C was approximately 26 min, when protein synthesis was disrupted by chloramphenicol; however, the activity remained constant when protein synthesis was not inhibited. From these results we concluded that catechol 2,3-dioxygenase from Bacillus thermoleovorans A2 is not particularly thermostable, but that the organism retains the ability to degrade phenol at high temperatures because of continuous production of this enzyme. Received: October 10, 1998 / Accepted: March 18, 1999     

Immobilization and stabilization of d-hydantoinase from Vigna angularis and its use in the production of N-carbamoyl-d-phenylglycine. Improvement of the reaction yield by allowing chemical racemization of the substrate

This work reports the immobilization of a multimeric d-hydantoinase (DHTase) from Vigna angularis (E.C. 3.5.2.2.) on agarose beads activated with glyoxyl groups aiming to improve its stability via multipoint covalent attachment. The final reduction with sodium borohydride resulted in a drop in enzyme activity that could be decreased by adding Zn²⁺ or Mg²⁺. The optimal preparation with high activity (58 % recovered activity) and stability (around 86-fold more stable than the free enzyme) was obtained by DHTase immobilization on glyoxyl agarose for 24 h at 25 °C and pH 10.05, and a borohydride reduction step in the presence of 10 mM Zn²⁺ (DHTase-Glx). The enzyme was almost fully immobilized on glyoxyl agarose (19.8 mg/g of support) when offering 20 mg/g. This immobilized biocatalyst was used to catalyze the hydrolysis of d,l-phenylhydantoin under substrate racemization conditions, which produced 99 % of N-carbamoyl-d-phenylglycine after 9 h reaction.     

恶臭假单胞菌ND6菌株catA基因的克隆和表达及其儿茶酚裂解途径探讨

恶臭假单胞菌ND6菌株的萘降解质粒pND6-1中编码儿茶酚1,2-双加氧酶的catA基因在大肠杆菌中进行了克隆和表达,并研究表达产物的酶学性质。结果表明:酶的K_m为0.019μmol/L,V_max为1.434μmol/(min.mg);具有很好的耐热性,在50℃保温45min后仍能够保留酶活力的93.7%;Fe²⁺对酶活性有显著的促进作用,其比活力是对照反应的292%;酶对4-氯儿茶酚的催化活性非常低,属于Ⅰ型儿茶酚1,2-双加氧酶。以萘为底物生长时,ND6菌株的细胞提取液中既存在催化邻位裂解途径的儿茶酚1,2-双加氧酶活性,也存在催化间位裂解途径的儿茶酚2,3-双加氧酶活性。以苯甲酸、对羟基苯甲酸和苯乙酸为唯一碳源生长时,ND6菌株细胞提取液的儿茶酚1,2-双加氧酶活性远远大于儿茶酚2,3-双加氧酶活性。表明ND6菌株既能通过儿茶酚间位裂解途径降解萘,也能通过儿茶酚邻位裂解途径降解萘,而以苯甲酸、对羟基苯甲酸和苯乙酸为诱导物时只利用儿茶酚邻位裂解途径。     

Characterization and evaluation of Aspergillus oryzae lactase coupled to a regenerable support

A derivative of crosslinked Sepharose, p-(N-acetyl-L-tyrosine azo) benzamidoethyl-CL-Sepharose 4B, was synthesized and used for the selective immobilization of thermostable lactase from Aspergillus oryzae.Preparations of soluble and immobilized lactase were evaluated under initial velocity conditions in a batch process. Immobilization had no significant effect on the pH optimum at 50 degrees C or kinetic parameters at pH 4.5 or pH 6.5 and 50 degrees C. At pH 4.5, the soluble enzyme possessed maximum activity at 60 degrees C and the immobilized at 55 degrees C; at pH 6.5 both showed maximum activity at 55 degrees C. The activation energy, entropy, and enthalpy decreased significantly with immobilization at pH 4.5 but not at pH 6.5. When the immobilized enzyme was placed in a packed-bed reactor, the effect of temperature on activity was altered as reflected by a marked decrease in the thermodynamic parameters of activation at both pH levels. Upon immobilization there was also a dramatic increase in the apparent thermal stability of the lactase, and the mean half-life at 50 degrees C was increased from 7.2 to 13 days at pH 4.5 and from 3.8 to 16 days at pH 6.5.     

Enhancement of starch conversion efficiency with free and immobilized pullulanase and alpha-1,4-glucosidase

Glucoamylase and pullulanase were immobilized on reconstituted bovine-hide collagen membranes using the covalent azide linkage method. A pretanning step was incorporated into the immobilization procedure to enable the support matrix to resist proteolytic activity while accommodating an operating temperature of 50 degrees C. The immobilized glucoamylase and pullulanase activities were 0.91 and 0.022 mg dextrose equivalent (DE) min(-1) cm(-2) of membrane, respectively. Immobilized glucoamylase had a half-life of 50 days while the immobilized pullulanase had a half-life of 7 days. This is a considerably improved stability over that reported by other researchers. The enzymes were studied in their free and immobilized forms on a variety of starch substrates including waxy maize, a material which contains 80% alpha-1-6-glucosidic linkages. Substrate concentrations ranged from 1% to a typical commercial concentration of 30%. Conversion efficiencies of 90-92% DE were obtained with free and immobilized glucoamylase preparations. Conversion enhancements of 4-5 mg of DE above this level were obtained by the use of pullulanase in its free or immobilized forms. Close examination of free pullulanase stability as a function of pH indicated improved thermal stability at higher pH values. At 50 degrees C and pH 5.0, the free enzyme was inactivated after 24 h. At pH 7.0, the enzyme still possessed one-half its activity after 72 h. Studies were conducted in both batch and continuous total recycle reactors. All experiments were conducted at 50 degrees C. Experiments conducted with coimmobilized enzymes proved quite promising. Levels of conversion equivalent to those obtained with the individually immobilized enzymes were realized.     

Immobilization and characterization of D-amino acid oxidase.

Optimal conditions with respect to pH, concentration of glutaraldehyde and enzyme, and order of addition of enzyme and crosslinking reagent were established for the immobilization of hog kidney D-amino acid oxidase to an attapulgite support. Yields of 40 to 70% were generally attained although when low concentrations of enzyme were used yields were consistently greater than 100%. It is suggested that this is due to a dimer leads to monomer shift at low protein concentrations. The stability of soluble D-amino acid oxidase was dependent on the buffer in which it was stored (pyrophosphate-phosphate greater than borate greater than Tris). Stability of immobilized enzyme was less than soluble in pyrophosphate-phosphate buffer, but storage in the presence of FAD improved stability. In addition, treatment of stored, immobilized enzyme with FAD before assay restored some of its activity. The immobilized D-amino acid oxidase was less stable to heat (50 degrees C) than the soluble enzyme from pH 6 to 8 but was more stable above and below these values. Apparent Km values for D-alanine, D-valine, and D-tryptophan decreased for the immobilized enzyme compared to the soluble.     

Purification and properties of pyrocatechase II from Pseudomonas putida strain 87]

Induction of modified ortho-pathway enzymes (catechol 1.2-dioxygenase II, muconate cycloisomerase II, dienelactone hydrolase, and maleylacetate reductase) was found in Pseudomonas putida 87, when 3-chlorobenzoic acid was used as a sole carbon and energy source. Catechol 1.2-dioxygenase II, the key chlorocatechol cleaving enzyme, was purified and characterized. The enzyme molecular mass as determined by gel filtration was 65,000 Da; the minimum molecular mass upon SDS electrophoresis was 33,000 Da. The pH and temperature optima for the enzyme were 7.2-7.8 and 35 degrees C, respectively. The highest stability of catechol 1.2-dioxygenase II upon storage was observed in 50 mM Tris-HCl buffer pH 7.8 at 4 degrees C. The relative values of Vmax for catechol 1.2-dioxygenase II with 3-chloro-, 4-chloro-, and 3.5-dichlorocatechols were 28%, 50%, and 41% of those for catechol. The enzyme affinity for chlorocatechols was 3-9 times higher than for methylcatechols and 10-20 times higher than for unsubstituted catechol.     

Protease produced by Pseudomonas aeruginosa K-187 and its application in the deproteinization of shrimp and crab shell wastes

In addition to chitinase/lysozyme, Pseudomonas aeruginosa K-187 also produced a protease useful for the deproteinization of shrimp and crab shell wastes. The optimal culture conditions for P. aeruginosa K-187 to attain the highest protease activity were investigated and discussed. The highest protease activity was as high as 21.2 U/ml, 10-fold that (2.2 U/ml) obtained prior to optimization. The protease of P. aeruginosa K-187, produced under the optimal culture conditions, was tested for crustacean waste deproteinization. The percent of protein removal for shrimp and crab shell powder (SCSP) after 7-day incubation was 72%, while that of natural shrimp shell (NSS) and acid-treated SCSP was 78% and 45%, respectively. In contrast, with the protease produced under pre-optimization conditions, the percent of protein removal for SCSP, NSS, and acid-treated SCSP was 48%, 55%, and 40%, respectively. For comparison, three other protease-producing microbes were tested for crustacean waste deproteinization. However, they were shown to be less efficient in deproteinization than P. aeruginosa K-187. The crude protease produced by P. aeruginosa K-187 can be covalently immobilized on a reversibly soluble polymeric support (hydroxypropyl methycellulose acetate succinate). The immobilized enzyme was soluble above pH 5.5 but insoluble below pH 4.5. Immobilization efficiency was 82%. The immobilized enzyme was stable between pH 6 and 9 and at temperatures below 60 degrees C. The optimum pH and temperature for the immobilized enzyme was pH 8 and 50 degrees C. The half-life of the immobilized enzyme was 12 days, longer than that of free protease (8 days). The utilization of the immobilized enzyme for the deproteinization of SCSP has resulted in a 67% protein removal. By contrast, SCSP protein removal by using free enzymes was 72%. The protease was further purified and characterized. The purification steps included ammonium sulfate precipitation, DEAE-Sepharose CL-6B ion-exchange chromatography, and Sephacryl S-200 gel-permeation chromatography. The enzyme had a molecular weight estimated to be 58.8 kDa by using sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The purified enzyme was active from pH 7 to 9 and its optimal pH was 8.     

Preparation and properties of an immobilized pectinlyase for the treatment of fruit juices

Pectinlyase, present in different commercial pectinases used in juice technology, was immobilized on alginate beads. The optimal conditions were: 0.17 g alginate ml(-1), 1.2% (w/v or v/v) enzyme concentration and acetic-HCl/glycine-HCl buffer at pH 3.6 or tris-HCl/imidazole buffer at pH 6.4. Maximum percentage of immobilization (10.6%) was obtained with Rapidase C80. Kinetic parameters of free and immobilized pectinlyase were also determined. The pH and temperature at which activity of soluble and immobilized enzyme was maximum were 7.2 and 55 degrees C. Thermal stability was not significantly altered by immobilization, especially at 40 degrees C, showing two periods of different stability. Free and immobilized preparation reduced the viscosity of highly esterified pectin from 1.09 to 0.70 and 0.72 mm(2) s(-1), respectively, after 30 min at 40 degrees C. Furthermore, the immobilized enzyme could be re-used through 4 cycles and the efficiency loss in viscosity reduction was found to be only 9.2%.     

Stabilization of soluble and immobilized horse liver alcohol dehydrogenase by adenosine 5'-monophosphate

Horse liver alcohol dehydrogenase, which catalyzes oxidoreductions for a broad spectrum of substrates of organic chemical interest, was immobilized on CNBr-activated Sepharose and on decylamine-substituted agarose. The specific activities of the immobilized enzyme preparations were compared with the free enzyme, and the apparent K(m) values of the preparations were determined for a selection of substrates. At pH 9 and 60 degrees C, soluble liver alcohol dehydrogenase was rapidly inactivated, while the enzyme immobilized on CNBr-activated Sepharose was more stable. Adenosine monophosphate (AMP), adenosine diphosphate, and adenosine diphosphoribose protected the free and immobilized alcohol dehydrogenase against heat inactivation. On storage under a variety of conditions, AMP effectively stabilized free horse liver alcohol dehydrogenase and the immobilized preparations.     

Glucose oxidase immobilization on a novel cellulose acetate-polymethylmethacrylate membrane

Glucose oxidase (GOD) was immobilized on cellulose acetate-polymethylmethacrylate (CA-PMMA) membrane. The immobilized GOD showed better performance as compared to the free enzyme in terms of thermal stability retaining 46% of the original activity at 70 degrees C where the original activity corresponded to that obtained at 20 degrees C. FT-IR and SEM were employed to study the membrane morphology and structure after treatment at 70 degrees C. The pH profile of the immobilized and the free enzyme was found to be similar. A 2.4-fold increase in Km value was observed after immobilization whereas Vmax value was lower for the immobilized GOD. Immobilized glucose oxidase showed improved operational stability by maintaining 33% of the initial activity after 35 cycles of repeated use and was found to retain 94% of activity after 1 month storage period. Improved resistance against urea denaturation was achieved and the immobilized glucose oxidase retained 50% of the activity without urea in the presence of 5M urea whereas free enzyme retained only 8% activity.     

Plasmid inheritability and biomass production: comparison between free and immobilized cell cultures of Escherichia coli BZ18(pTG201) without selection pressure.

Maintenance of the plasmid pTG201 in Escherichia coli BZ18 was studied for both free and immobilized cells during chemostat culture, in the absence of the antibiotic against which resistance was plasmid encoded. Electron microscopic observations of immobilized proliferant cells within carrageenan gel beads showed high cell concentrations and growth into distinct cavities. The plasmid which coded for the catechol 2,3-dioxygenase activity was stably maintained during 80 generations in the case of immobilized cells. A theoretical analysis founded on the compartmentalization resulting from the immobilized growth conditions was described. However, the model still showed a plasmid stability inferior to that determined experimentally. Hypotheses dealing with physiological changes of immobilized cells were presented. In addition, the high cell concentrations obtained in the outer 50 microns of the carrageenan gel beads gave a biomass productivity within this useful volume which was 20 times higher than in free-cell cultures.     

Kinetics and stability of immobilized chicken liver xanthine dehydrogenase.

Xanthine dehydrogenase (EC 1.2.1.37) was isolated from chicken livers and immobilized by adsorption to a Sepharose derivative, prepared by reaction of n-octylamine with CNBr-activated Sepharose 4B. Using a crude preparation of enzyme for immobilization it was observed that relatively more activity was adsorbed than protein, but the yield of immobilized activity increased as a purer enzyme preparation was used. As more activity and protein were bound, relatively less immobilized activity was recovered. This effect was probably due to blocking of active xanthine dehydrogenase by protein impurities. The kinetics of free and immobilized xanthine dehydrogenase were studied in the pH range 7.5-9.1. The Km and V values estimated for free xanthine dehydrogenase increase as the pH increase; the K'm and V values for the immobilized enzyme go through a minimum at pH 8.1. By varying the amount of enzyme activity bound per unit volume of gel, it was shown that K'm is larger than Km are result of substrate diffusion limitation in the pores of the support material. Both free and immobilized xanthine dehydrogenase showed substrate activation at low concentrations (up to 2 microM xanthine). Immobilized xanthine dehydrogenase was more stable than the free enzyme during storage in the temperature range of 4-50 degrees C. The operational stability of immobilized xanthine dehydrogenase at 30 degrees C was two orders of magnitude smaller than the storage stability, t 1/2 was 9 and 800 hr, respectively. The operational stability was, however, better than than of immobilized milk xanthine oxidase (t 1/2 = 1 hr). In addition, the amount of product formed per unit initial activity in one half-life, was higher for immobilized xanthine dehydrogenase than for immobilized xanthine oxidase. Unless immobilized milk xanthine oxidase can be considerable stabilized, immobilized chicken liver xanthine dehydrogenase is more promising for application in organic synthesis.     

Reversible thermal denaturation of immobilized rhodanese

For the first time, the enzyme rhodanese had been refolded after thermal denaturation. This was previously not possible because of the strong tendency for the soluble enzyme to aggregate at temperatures above 37 degrees C. The present work used rhodanese that was covalently coupled to a solid support under conditions that were found to preserve enzyme activity. Rhodanese was immobilized using an N-hydroxymalonimidyl derivative of Sepharose containing a 6-carbon spacer. The number of immobilized competent active sites was measured by using [35S]SO3(2-) to form an active site persulfide that is the obligatory catalytic intermediate. Soluble enzyme was irreversibly inactivated in 10 min at 52 degrees C. The immobilized enzyme regained at least 30% of its original activity even after boiling for 20 min. The immobilized enzyme had a Km and Vmax that were each approximately 3 times higher than the corresponding values for the native enzyme. After preincubation at high temperatures, progress curves for the immobilized enzyme showed induction periods of up to 5 min before attaining apparently linear steady states. The pH dependence of the activity was the same for both the soluble and the immobilized enzyme. These results indicate significant stabilization of rhodanese after immobilization, and instabilities caused by adventitious solution components are not the sole reasons for irreversibility of thermal denaturation seen with the soluble enzyme. The results are consistent with models for rhodanese that invoke protein association as a major cause of inactivation of the enzyme. Furthermore, the induction period in the progress curves is consistent with studies which show that rhodanese refolding proceeds through intermediate states.     

Preparation and properties of immobilized papain and lipase.

Papain and lipase were immobilized on derivatized Sepharose 4-B. The activated agarose had a binding capacity of 1.2 micronmol amino groups/ml packed agarose or 17 mg proteins/g dry agarose. The immobilized enzyme preparations were tested for the effects of pH of assay, temperature of assay, and substrate concentrations. The effect of 6M urea on the activity of papain was also determined. Soluble forms of the enzymes were used for comparison. Immobilization of the enzymes resulted in slightly different pH and temperature optima for activities. For immobilized papain Km(app) was similar to the one observed with soluble papain. Immobilization of lipase, however, cause a decrease in Km values. The immobilized enzyme preparations were stable when stored at 4 degrees C and pH 7.5 for periods up to eight months. The soluble enzymes lost their activity within 96 hr under similar storage conditions. Immobilized papain did not lose any activity after treatment with 6M urea for 270 min, whereas soluble papain lost 81% of its activity after the urea treatment, indicating that the immobilization of papain imparted structural and conformational stability to this enzyme.     

产胞外邻苯二酚1.2—双加氧酶的菌种筛选和发酵条件的研究

Two strains of Pseudomonus sp. having the extracellular catechol 1, 2-dioxygenase activity were selected from 112 bacterial strains. The conditions for enzyme production of the strains were examined. The optimal temperature and pH for enzyme formation were 30 degrees C and pH 6.8-7.0 respectively. Enzyme formation was enhanced by sodium benzoate, and was markedly inhibited by glucose, maltose and glycerol. Ammoniacal nitrogen sources were essential for cell growth and enzyme production. Sodium succinate was an effective inducer for enzyme formation. When the organism was grown in 0.15% sodium benzoate medium (pH 6.8-7.0) at 30 degrees C for 72 hours, about 10 units of catechol 1,2 dioxygenase per ml was obtained.     

Phenol Degradation by Immobilized Cells of Arthrobacter citreus

An aerobic microorganism with an ability to utilize phenol as carbon and energy source was isolated from a hydrocarbon contamination site by employing selective enrichment culture technique. The isolate was identified as Arthrobacter citreus based on morphological, physiological and biochemical tests. This mesophilic organism showed optimal growth at 25°C and at pH of 7.0. The phenol utilization studies with Arthrobacter citreus showed that the complete assimilation occurred in 24 hours. The organism metabolized phenol up to 22 mM concentrations whereas higher levels were inhibitory. Thin layer chromatography, UV spectral and enzyme analysis were suggestive of catechol, as a key intermediate of phenol metabolism. The enzyme activities of phenol hydroxylase and catechol 2,3-dioxygenase in cell free extracts of Arthrobacter citreus were indicative of operation of a meta-cleavage pathway for phenol degradation. The organism had additional ability to degrade catechol, cresols and naphthol. The degradation rates of phenol by alginate and agar immobilized cells in batch fermentations showed continuous phenol metabolism for a period of eight days.