New method of immobilization of microbial cells by capture on the surface of insoluble pyridinium-type resin

A new method for the immobilization of microbial cells has been developed. Whole cells of Escherichia coli with aspartase activity were immobilized by capture on the surface of cross-linked poly(N-benzyl-4-vinylpyridinium bromide) containing styrene (BVPS resin), an insoluble pyridinium-type resin. When a suspension of the bacterial cells in buffer solution was passed through a glass column containing beads of BVPS resin, the cells were captured on the resin surface and formed an immobilized cell system. A fixed-bed column reactor containing 300 mg of the bacterial cells immobilized by capture on 10 g of BVPS resin beads was used for the preparation of L-aspartic acid from ammonium fumarate. Continuous operation of tne bioreactor produced L-aspartic acid in a quantitative yield when the influent substrate concentration was 0.1M and the flow rate was 0.41-0.83 bed volumes per hour at pH 7.4-7.7 at 30 degrees C.     

Continuous production of L-aspartic acid by immobilized aspartase

Various methods were tried for the immobilization of aspartase, and the preparation having the highest activity was obtained when partially purified aspartase from Escherichia coli was entrapped into polyacrylamide gel Iattice. Enzymatic properties of the immobilized aspartase were investigated and compared with those of the native aspartase. With regard to optimum pH, temperature, concentration of Mn⁺⁺, kinetic constants and heat stability, no marked difference was observed between the native and immobilized aspartases. By employing an enzyme column packed with the immobilized aspartase, conditions for continuous production of L -aspartic acid from ammonium fumarate were investigated. When a solution of 1M ammonium fumarate (pH 8.5, containing 1mM MnCl₂) was passed through the aspartase column at the flow rate of SV = 0.08 at 37°C, the highest rate of reaction was attained. From the column effluents, L-aspartic acid was obtained in a good yield.     

Immobilized cells of recombinant Escherichia coli strain for continuous production of L-aspartic acid

For L-aspartic acid biosynthesis, high production cells of Escherichia coli mutant B-715 and P1 were immobilized in chitosan gel using a technique developed in our laboratory. The immobilization process reduced initial activity of the intact cells, however, the biocatalyst produced was very stabile for long-term use in multi-repeated batch or continuous processes. Temperature influence on the conversion of ammonium fumarate to L-aspartic acid was investigated. In long-term experiments, over 603 hours, the temperature 40 degrees C was found to be the best for both biocatalyst stability and high conversion rate. The optimum substrate concentration was 1.0 M. Continuous production of L-aspartic acid was investigated in three types of column bioreactors characterized by different volumes as well as different high to biocatalyst bed volume rations (Hz/Vz). The highest conversion rate, 99.8%, and the productivity 6 g/g/h (mass of L-aspartic acid per dry mass of cells in biocatalyst per time unit) was achieved in the bioreactor with the highest value Hz/Vz = 3.1, and liquid hour space velocity value of 5.2, defined as the volume of feeding substrate passed per volume of catalyst in bioreactor per one hour.     

Immobilization of Escherichia coli Cells Containing Aspartase Activity with Polyurethane and Its Application for l-Aspartic Acid Production

Whole cells of Escherichia coli containing aspartase activity were immobilized by mixing a cell suspension with a liquid isocyanate-capped polyurethane prepolymer (Hypol). The immobilized cell preparation was used to convert ammonium fumarate to l-aspartic acid. Properties of the immobilized E. coli cells containing aspartase were investigated with a batch reactor. A 1.67-fold increase in the l-aspartic acid production rate was observed at 37 degrees C as compared to 25 degrees C operating temperature. The pH optimum was broad, ranging from 8.5 to 9.2. Increasing the concentration of ammonium fumarate to 1.5 M from 1.0 M negatively affected the reaction rate. l-Aspartic acid was produced at an average rate of 2.18 x 10 mol/min per g (wet weight) of immobilized E. coli cells with a 37 degrees C substrate solution consisting of 1.0 M ammonium fumarate with 1 mM Mg (pH 9.0).     

Stability of the biocatalysts of L-aspartic acid synthesis based on immobilized Escherichia coli cells

Experiments were carried out to investigate the process of a continuous enzymatic synthesis of L-aspartic acid from ammonium fumarate in uniform filling flow reactors. Escherichia coli (Soviet strain 85) cells immobilized in polyacrylamide gel granules reinforced by a solid carrier were used as biocatalysts. The conditions, under which a high aspartase activity of the biocatalyst and a stable hydrodynamic performance of the reactor were maintained, were determined. The main kinetic characteristics of a continuous performance of the reactor for 150 days were obtained.     

Production of L-aspartic acid from fumaric acid by a fumaric acid-assimilating obligate thermophile,Bacillus stearothermophilus KP 1041

Summary A fumaric acid-assimilating obligate thermophile having a high aspartase activity was isolated from soil. The isolate (KP 1041) that grew at 45 to 68 °C was assigned to a strain of Bacillus stearothermophilus. The cell suspensions produced L-aspartate from fumarate and ammonium ion, with the rapidest initial rate at 65 °C and pH 9.5. The Michaelis constant for fumarate was 0.2 M. The cellular aspartase was relatively stable for 18 h at and below 50 °C over a pH range 6.7–8.3 in the presence of ammonium fumarate; this substance protected the enzyme from heat inactivation. The best yield in L-aspartic acid production was achieved at 6 h incubation at 53 °C and pH 8.5, using 0.88 M fumarate, 3.1 M ammonium ion, and the cells at 53 mg dry weight per ml. In this case, 85% of fumarate added was converted into aspartic acid. The structure of the product was determined from its infrared spectrum, specific rotation, melting point and ultimate analysis.Presented at the Annual Meeting of the Agricultural Chemical Society of Japan, Yokohama, April 2, 1977     

Continuous production of l-aspartic acid from ammonium fumarate using immobilized cells by capture on the surface of nonwoven cloth coated with a pyridinium-type polymer

Cells of Escherichia coli possessing aspartase activity were immobilized by capture on the surface of nonwoven cloth coated with 10 mg/g of poly (N-benzyl-4-vinylpyridinium chloride-co-styrene), a pyridinium-type polymer. Continuous operation of a fixed-bed column reactor containing 21.7 g/l of the immobilized cells produced l-aspartic acid in 95% yield from ammonium fumarate in the case where influent solution contained 0.1 mol/l of the fumarate and space velocity was 1.36 h⁻¹ at 30°C and pH 8.9. Immobilization on the coated nonwoven cloth insignificantly affected optimal pH of the biochemical reaction. Stability of enzymic activity of the immobilized cells was much improved by use of the coated nonwoven cloth as the supporting material instead of beads of insoluble pyridinium-type resin. l-Aspartic acid was obtained in 77% yield after 160 d of continuous operation, and the initial yield was estimated to require about 500 d for halving.     

疏水吸附固定化天冬氨酸酶及其性质的研究

本文论述了一种N-烷基琼脂珠衍生物的合成方法,研究了pH,离子强度、载体上疏水基团含量等因素对载体吸附天冬氨酸酶的影响以及固定化天冬酸酶的性质。结果表明邻甲苯胺基琼脂珠在pH5.5,0.1mol/L磷酸缓冲液(含有0.25mol/LKCL)中,每克湿载体可吸附15—25mg酶蛋白,酶活力回收达90％以上。固定化酶的性质有所改变,其热稳定性和操作稳定性明显增强。 固定化天冬氨酸酸柱可以用于连续化生产L-天冬氮酸,在pH8.0,1.0mol/L及丁烯二酸铵(含0.02mol/L MgCl_2),30℃条件下,以空间流速SV=3.5操作2个月,固定化酶活力仍保持79.5％。     

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     

Preparation of L-aspartic acid by means of immobilized Alcaligenes metalcaligenes cells

Two types of biocatalysts based on immobilized cells of Alcaligenes metalcaligenes exhibiting aspartate ammonia-lyase activity (EC 4.3.1.1) were developed for the enzymic preparation of L-aspartic acid from ammonium fumarate. The first type of the biocatalyst consists in individual covalently crosslinked and permeabilized cells(I), while the second type is represented by cell aggregates (II). For the above preparation, biocatalyst I can be used only discontinuously in a mixed reactor. After termination of the reaction between individual cycles of its use, the biocatalyst is returned to the reactor in the form of a highly concentrated cell suspension or paste. Biocatalyst II can be used discontinuously or continuously in a fixed-bed column of the catalyst. The effects of pH, substrate concentration and temperature on the reaction velocity and effectivity of enzymic conversion was investigated. Optimal parameters of the reaction are as follows: pH 8.5, initial substrate concentration, 1.35 mol/L, temperature for discontinuous process, 37 degrees C, and temperature for continuous process, 25 degrees C. Under these conditions the enzymic conversion of substrate to product is quantitative. Under optimal toring conditions, the specific activity of both catalysts does not change within a period of one year. The operational half-life of the biocatalyst II during continuous use in a fixed-bed column of the catalyst under standard reaction conditions depends on the quality of the substrate. The discontinuous preparation of L-asparatic acid with the aid of biocatalyst I and continuous preparation of this product with the aid of biocatalyst II have been verified under pilot-plant conditions.     

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.     

Continuous itaconic acid production by immobilized biocatalysts.

The continuous itaconic acid production from sucrose with Aspergillus terreus TKK 200-5-3 mycelium immobilized on polyurethane foam cubes was optimized in column bioreactors using statistical experimental design and empirical modelling. The highest itaconic acid product concentration calculated on the basis of the obtained model was 15.8 g l-1 in the investigated experimental area, when sucrose concentration was 13.5%, aeration rate 150 ml min-1 and residence time 178 h. From sucrose with immobilized A. terreus TKK 200-5-3 mycelium itaconic acid production was stable for at least 4.5 months in continuous column bioreactors. In comparison, using glucose as substrate and immobilized A. terreus TKK 200-5-1 mycelium as biocatalyst similar stability was obtained with higher product concentration. The omission of copper sulphate from the production medium gave the highest itaconic acid product concentration (26 g l-1) from 9% glucose with 0.25% ammonium nitrate and 0.095% magnesium sulphate.     

Thermodynamics of the conversion of aqueous L-aspartic acid to fumaric acid and ammonia

The thermodynamics of the conversion of aqueous L-aspartic acid to fumaric acid and ammonia have been investigated using both heat conduction microcalorimetry and high-pressure liquid chromatography. The reaction was carried out in aqueous phosphate buffer over the pH range 7.25-7.43, the temperature range 13-43 degrees C, and at ionic strengths varying from 0.066 to 0.366 mol kg(-1). The following values have been found for the conversion of aqueous L-aspartateH- to fumarate2- and NH4+ at 25 degrees C and at zero ionic strength: K = (1.48 +/- 0.10) x 10(-3), DeltaG degrees = 16.15 +/- 0.16 kJ mol(-1), DeltaH degrees = 24.5 +/- 1.0 kJ mol(-1), and DeltaC(p) degrees = -147 +/- 100 J mol(-1) K(-1). Calculations have also been performed which give values of the apparent equilibrium constant for the conversion of L-aspartic acid to fumaric acid and ammonia as a function of temperature, pH and ionic strength.     

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.     

Physical property improvements of a pellicular biocatalyst

The thermal stability of an immobilization technique using a pellicular latex matrix was examined in a packed-bed column reactor. The stability was found to vary with liquid flow rate, the type of latex, temperature of operation, and the amount of yeast cells. Adjusting these parameters and introducing particulate inorganic fillers strengthened the latex matrix and improved the thermal stability. Optimization of this immobilization technique resulted in a procedure that allowed latex polymers to be mechanically stable at temperatures up to 50°C. The biological viability of this improved immobilization scheme was demonstrated through the production of L-aspartic acid by immobilized cells of E. coli.     

Aspartic Acid Synthesis by <Emphasis Type="Italic">Escherichia coli</Emphasis> Strains with Deleted Fumarase Genes as Biocatalysts

The work reports the construction of Escherichia coli strain MG1655 derivatives with deleted genes that encode fumarases (fumAC, fumB, and fumABC) via the phage lambda-mediated recombination system. It has been demonstrated that the deletion of fumB gene had almost no effect on strain growth under aerobic conditions, while the deletion of the fumA and fumC genes led to a 30% decrease in the growth rate under the same conditions. When the E. coli strains with deleted fumarase genes were used to catalyze L-aspartic acid synthesis from ammonium fumarate (1.5 M solution), it was observed that only the simultaneous loss of both the fumA and fumC genes led to an at least 20% increase in the aspartic acid yields and a concurrent decrease in the content of the byproduct malic acid in the reaction mixture from 40 to 1.5–2 g/L. The results obtained in the work may be used to generate more efficient novel biocatalysts of L-aspartic acid synthesis.     

L-Malic acid production by polyacrylamide gel entrapped Pichia membranaefaciens

Summary The production of L-malic acid from fumaric acid has been achieved byPichia membraneafaciens cells entrapped in a polyacrylamide gel lattice. The reaction rate was found to be 0.15 mmoles/h/g of immobilized cells. The optimum pH for fumarase activity of immobilized cells was stable after repeated uses it increased after storing the gel pellets at 5°C. A good yield of L-malic acid production (up to 3.77 g/l) was also observed in wine added with Na fumarate.     

Electrochemical nucleic acid hybridization biosensor based on poly(L-Aspartic acid)-modified electrode for the detection of short oligonucleotide sequences related to hepatitis C virus 1a

Abstract

This work describes, for the first time, the fabrication of poly(L-aspartic acid) (PAA) film modified pencil graphite electrode (PGE) for the detection of hepatitis C Virus 1a (HCV1a). The presence of PAA on the electrode surface can provide free carboxyl groups for covalent binding of biomolecules. The PGE surface was first coated with PAA via electropolymerization of the L-aspartic acid, and avidin was subsequently attached to the PAA modified electrode by covalent attachment. Biotinylated HCV1a probes were immobilized on avidin/PAA/PGE via avidin-biotin interaction. The morphology of PAA/PGE was examined using a scanning electron microscope. The hybridization events were monitored with square wave voltammetry using Meldola’s blue (MDB). Compared to non-complementary oligonucleotide sequences, when hybridization was carried out between the probe and its synthetic targets or the synthetic polymerase chain reaction analog of HCV1a, the highest MDB signal was observed. The linear range of the biosensor was 12.5 to 100?nM and limit of detection was calculated as 8.7?nM. The biosensor exhibited favorable stability over relatively long-term storage. All these results suggest that PAA-modified electrode can be used to nucleic acid biosensor application and electropolymerization of L-aspartic acid can be considered as a good candidate for the immobilization of biomolecules.     

Improvement of production of l-aspartic acid using immobilized microbial cells

Summary In our laboratory, EAPc-7 a strain having higher aspartase activity was derived from Escherichia coli ATCC 11303. For the improvement of l-aspartic acid productivity using EAPc-7 cells immobilized in -carrageenan, it was necessary to eliminate the fumarase activity which converts fumaric acid to l-malic acid. Several treatments for specifically eliminating fumarase activity from EAPc-7 cells were tested and it was found that when EAPc-7 cells were treated in a culture broth (pH 4.9) containing 50 mM l-aspartic acid at 45° C for 1 h, fumarase activity was almost completely eliminated without inactivation of the aspartase.The treated cells, immobilized in -carrageenan, were used for continuous production of l-aspartic acid from ammonium fumarate. The formation of l-malic acid was negligible and the half-life of the immobilized preparation was 126 days.Productivity of immobilized preparation of treated EAPc-7 cells in l-aspartic acid production was six times of that of the parent cell preparation.     

Cellulose acetate entrapment of Escherichia coli on cotton cloth for aspartate production

Summary Aspartase containingEscherichia coli cells were entrapped in cellulose acetate aggregated on cotton cloth. The enzyme activity of the cloth was stabilized by treatment with polyethylenimine and alkaline glutaraldehyde in the presence of 0.1 M sodium dithionite. A column packed with the cloth segments catalyzed 100% conversion of 1 M ammonium fumarate to aspartic acid at a space velocity of 7/h. When the same cloth segments were stirred at 100 rpm in the substrate solution, the productivity of the cloth increased 2.5 times.