Lactic acid fermentation by cells of Lactobacillus rhamnosus immobilized in polyacrylamide gel

Summary The process of lactic acid fermentation of lactose to lactic acid by Lactobacillus rhamnosus ATCC 7469 has been studied. The following processes have been explored: growth kinetics, as well as lactose utilization, production of lactic acid and further degradation of lactic acid. The immobilization experiments were conducted with microbial cells entrapped in polyacrylamide gels. Gels with different ratios of the monomer (acrylamide) and the cross-linking agent (N,N′-methylene-bis-acrylamide) have been tested. These were used in a repeat-batch process. The current processes inside and outside the gel particles were subjects of examination. The evolution of the activity of immobilized cells with repeated use showed that the particles served mainly as a donor of cells for the free culture. In all experiments a very high degree of conversion, 85–90% was observed. After several runs however, the particles were exhausted for microbial cells. A kinetic model of the process of lactic acid production was developed. This model allowed the evaluation of the effect of microbial growth and diffusion limitations inside the gel particles on the process rate and the separate contribution of the free and immobilized cells to the overall fermentation process upon multiple use.     

Applicability of pectate-entrapped <Emphasis Type="Italic">Lactobacillus casei</Emphasis> cells for <Emphasis Type="SmallCaps">l</Emphasis>(+) lactic acid production from whey

Lactic acid is a versatile organic acid, which finds major application in the food, pharmaceuticals, and chemical industries. Microbial fermentation has the advantage that by choosing a strain of lactic acid bacteria producing only one of the isomers, an optically pure product can be obtained. The production of l(+) lactic acid is of significant importance from nutritional viewpoint and finds greater use in food industry. In view of economic significance of immobilization technology over the free-cell system, immobilized preparation of Lactobacillus casei was employed in the present investigation to produce l(+) lactic acid from whey medium. The process conditions for the immobilization of this bacterium using calcium pectate gel were optimized, and the developed cell system was found stable during whey fermentation to lactic acid. A high lactose conversion (94.37%) to lactic acid (32.95 g/l) was achieved with the developed immobilized system. The long-term viability of the pectate-entrapped bacterial cells was tested by reusing the immobilized bacterial biomass, and the entrapped bacterial cells showed no decrease in lactose conversion to lactic acid up to 16 batches, which proved its high stability and potential for commercial application.     

Bioconversion of acrylonitrile to acrylamide using polyacrylamide entrapped cells of <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> PA-34

The nitrile hydratase (NHase) of Rhodococcus rhodochrous PA-34 catalyzed the conversion of acrylonitrile to acrylamide. The resting cells (having NHase activity) (8 %; 1 mL corresponds to 22 mg dry cell mass, DCM) were immobilized in polyacrylamide gel containing 12.5 % acrylamide, 0.6 % bisacrylamide, 0.2 % diammonium persulfate and 0.4 % TEMED. The polyacrylamide entrapped cells (1.12 mg DCM/mL) completely converted acrylonitrile in 3 h at 10 °C, using 0.1 mol/L potassium phosphate buffer. In a partitioned fed batch reactor, 432 g/L acrylamide was accumulated after 1 d. The polyacrylamide discs were recycled up to 3×; 405, 210 and 170 g/L acrylamide was produced in 1st, 2nd and 3rd recycling reactions. In four cycles, a total of 1217 g acrylamide was produced by recycling the same mass of entrapped cells.     

Synthesis of l-tyrosine by immobilized Escherichia intermedia cells

Summary Cells of Escherichia intermedia were immobilized by entrapment in a polyacrylamide gel and used for the enzymatic production of l-tyrosine from phenol, pyruvate, and ammonia. A preparation containing 50 mg of cells/g of gel retained 60% of its original activity. The effect of temperature, pH and substrate concentration on the activity of free cells was almost identical with the effect on immobilized cells. Phenol showed inhibition and inactivation of the catalyst at high concentration. Synthesis of l-tyrosine (up to 10 g/l) was demonstrated in batch reactors with high conversion yields (95–100%) and a maximal productivity of 2 g/l/h. In continuous reactor the catalyst showed a very high operational stability (more than 54 days without losses).     

Immobilization of <Emphasis Type="Italic">Streptomyces</Emphasis> phospholipase D on a Dowex macroporous resin

The immobilization of phospholipase D produced by Streptomyces sp. YU100 was evaluated to see it would be practical for industrial applications. To accomplish this, the purified enzyme, which contained 53 unit/mg of protein, was subjected to immobilization on various matrices. When immobilization supports including calcium alginate gel, polyacrylamide gel, and macroporous resin were evaluated, the highest enzyme retention ratio (> 42%) was observed on a Dowex MSA-2 macro-porous resin. This may have occurred as a result of the ability of the hydrophobic domain of phospholipase D to interact with the polystyrene backbone of the resin, as well as the ability of the dimethylethanolamine group of the MSA-2 resin to retain the enzyme by forming hydrogen bonds with the acidic residues of the enzyme. Upon the operation of a reactor packed with enzyme that had been immobilized on a Dowex MSA-2 resin, greater than 80% of the initial enzyme activity was retained for 16 days. During the reaction, phosphatidylcholine became bound to the immobilized resin and interfered with the enzyme reaction, therefore, the resin was washed with ethyl ether every 2 h. A process for recovering excessive l-serine from phospholipids using the Dowex MR-3 resin was designed, and the separated l -serine was employed again after replacing the amount that was used.     

Production of l (+) lactic acid by Lactobacillus delbrueckii immobilized in functionalized alginate matrices

The role of functionalized alginate gels as immobilized matrices in production of l (+) lactic acid by Lactobacillus delbrueckii was studied. L. delbrueckii cells immobilized in functionalized alginate beads showed enhanced bead stability and selectivity towards production of optically pure l (+) lactic acid in higher yields (1.74Yp/s) compared to natural alginate. Palmitoylated alginate beads revealed 99% enantiomeric selectivity (ee) in production of l (+) lactic acid. Metabolite analysis during fermentation indicated low by-product (acetic acid, propionic acid and ethanol) formation on repeated batch fermentation with functionalized immobilized microbial cells. The scanning electron microscopic studies showed dense entrapped microbial cell biomass in modified immobilized beads compared to native alginate. Thus the methodology has great importance in large-scale production of optically pure lactic acid.     

Immobilization of <Emphasis Type="Italic">Escherichia coli</Emphasis> cells with <Emphasis Type="Italic">cis</Emphasis>-epoxysuccinate hydrolase activity for <Emphasis Type="SmallCaps">d</Emphasis>(−)-tartaric acid production

Immobilization of cis-epoxysuccinate hydrolase-containing E. coli for d(−)-tartaric acid production was screened by various methods. The highest recovery of activity was obtained by entrapment in κ-carrageenan gel. 23.6 g biomass/l and 43.4 g κ-carrageenan/l were the best immobilization conditions optimized by response surface methodology with 83% yield (114 U/g). Cell autolysis was observed after immobilization. Immobilized cells showed high pH (5–10) stability, thermal (up to 65°C) stability, conversion rate (>99.5%), enantioselectivity (ee > 99.6%), and were less affected by metal ions and surfactants compared with free cells. Conversion rate for immobilized cells preserved 93% after 10 repeated batches (5% for free cells).     

Cu2+ Removal and recovery by Spi SORB: batch stirred and up-flow packed bed columnar reactor systems

The biosorption of Cu²⁺ by free and poly acrylamide gel (PAG) immobilized Spirulina platensis (SpiSORB) was characterized under batch and continuous packed bed columnar reaction systems. The biosorption of Cu²⁺ was shown to be highest at pH of 6.0 for both types of biomass. The PAG immobilization process did not interfere with the Cu²⁺ binding sites present on biomass leading to cent percent (ca. 250 mg g⁻¹ of dry biomass) retention of biosorption as compared to free cells. Transmission electron microscopy on Cu²⁺ localization revealed that majority of metal is being sequestered by the cell wall only. The infrared spectrum of metal treated S. platensis biomass indicated the possible involvement of amide, amino, and carboxyl groups in metal binding. Up-flow packed bed columnar reactor containing 2.0 g of PAG immobilized S. platensis shown a maximum of 143-fold volume reduction factor at the residence time of 4.6 min for Cu²⁺ alone and found to decrease dramatically when Zn²⁺ is present in a bimetallic solution.     

Acrylamide synthesis using agar entrapped cells of <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> PA-34 in a partitioned fed batch reactor

The nitrile hydratase (Nhase) induced cells of Rhodococcus rhodochrous PA-34 catalyzed the conversion of acrylonitrile to acrylamide. The cells of R. rhodochrous PA-34 immobilized in 2% (w/v) agar (1.76 mg dcw/ml agar matrix) exhibited maximum Nhase activity (8.25 U/mg dcw) for conversion of acrylonitrile to acrylamide at 10°C in the reaction mixture containing 0.1 M potassium phosphate buffer (pH 7.5), 8% (w/v) acrylonitrile and immobilized cells equivalent to 1.12 mg dcw (dry cell weight) per ml. In a partitioned fed batch reaction at 10°C, using 1.12 g dcw immobilized cells in a final volume of 1 l, a total of 372 g of acrylonitrile was completely hydrated to acrylamide (498 g) in 24 h. From the above reaction mixture 87% acrylamide (432 g) was recovered through crystallization at 4°C. By recycling the immobilized biocatalyst (six times), a total of 2,115 g acrylamide was produced.     

A novel thermostable nitrilase superfamily amidase from <Emphasis Type="Italic">Geobacillus pallidus</Emphasis> showing acyl transfer activity

An amidase (EC 3.5.1.4) in branch 2 of the nitrilase superfamily, from the thermophilic strain Geobacillus pallidus RAPc8, was produced at high expression levels (20 U/mg) in small-scale fermentations of Escherichia coli. The enzyme was purified to 90% homogeneity with specific activity of 1,800 U/mg in just two steps, namely, heat-treatment and gel permeation chromatography. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) and electron microscopic (EM) analysis of the homogenous enzyme showed the native enzyme to be a homohexamer of 38 kDa subunits. Analysis of the biochemical properties of the amidase showed that the optimal temperature and pH for activity were 50 and 7.0°C, respectively. The amidase exhibited high thermal stability at 50 and 60°C, with half-lives greater than 5 h at both temperatures. At 70 and 80°C, the half-life values were 43 and 10 min, respectively. The amidase catalyzed the hydrolysis of low molecular weight aliphatic amides, with d-selectivity towards lactamide. Inhibition studies showed activation/inhibition data consistent with the presence of a catalytically active thiol group. Acyl transfer reactions were demonstrated with acetamide, propionamide, isobutyramide, and acrylamide as substrates and hydroxylamine as the acyl acceptor; the highest reaction rate being with isobutyramide. Immobilization by entrapment in polyacrylamide gels, covalent binding on Eupergit C beads at 4°C and on Amberlite-XAD57 resulted in low protein binding and low activity, but immobilization on Eupergit C beads at 25°C with cross-linking resulted in high protein binding yield and high immobilized specific activity (80% of non-immobilized activity). Characterization of Eupergit C-immobilized preparations showed that the optimum reaction temperature was unchanged, the pH range was somewhat broadened, and stability was enhanced giving half-lives of 52 min at 70°C and 30 min at 80°C. The amidase has potential for application under high temperature conditions as a biocatalyst for d-selective amide hydrolysis producing enantiomerically pure carboxylic acids and for production of novel amides by acyl transfer.     

Use of immobilized cells of Rhizopus nigricans for the 11α-hydroxylation of progesterone

The filamentous fungus, Rhizopus nigricans, was immobilized in polyacrylamide, alginate, and agar gels and its ability to 11α-hydroxylate progesterone was examined. No activity was detected using polyacrylamide gel but both agar and alginate gels have proved capable of hydroxylation. Agar gels displayed faster rates and higher yields. It was possible to induce hydroxylase synthesis within agar and alginate gels, and microscopical examination provided evidence for hyphal growth within these gels. The concept of increased biomass was used to explain the observed increase in the rates of hydroxylase activity of the immobilized cells. Conversely, hyphal overcrowding was postulated for the rapid inactivation observed under some operating conditions.     

Synthesis of l-dopa by escherichia intermedia cells immobilized in a polyacrylamide gel

Summary Escherichia intermedia cells were immobilized by entrapment in a polyacrylamide gel and used for l-dopa synthesis from pyrocatechol, pyruvate and ammonia. An immobilized cell preparation containing 75 mg cells/g gel retained 45%–50% of the activity of free cells. The effect of temperature, pH and substrate concentration of the initial rate of l-dopa synthesis was very similar for free and immobilized cells. Substrate inhibition was observed for pyrocatechol, pyruvate and ammonia. In a batch reactor, 5.4 g·l^-1 l-dopa was obtained, with 100% conversion yield of pyrocatechol and l-dopa productivity of 0.18 g·l^-1·h^-1. The use of a pyrocatechol-borate complex decreased by-product formation and catalyst inactivation.     

Protease production by immobilized mycelia of Streptomyces fradiae

Streptomyces fradiaewas immobilized in polyacrylamide gel prepared from 5% total acrylamide (90% acrylamide and 10%N,N′-methylenebisacrylamide). Production of protease by the immobilized mycelia was attempted in a batch system. A dilute medium containing 0.5% starch, 0.5% meat extract, and 0.05% yeast extract was employed. The reusability of the immobilized and washed mycelia was examined. The activity of protease production by washed mycelia was rapidly decreased with increasing use cycles. The activity of the immobilized mycelia increased gradually, and reached a maximum after ten use cycles. Then, the activity gradually decreased with increasing reaction cycles. This might be caused by destruction of the gels. On the other hand, the sterilization of the surface of the immobilized mycelia was effective for elongation of the lifetime. As a result, the half-life of protease production by the sterilized immobilized mycelia was about 30 days. The rate of protease production by immobilized mycelia was 12,000 U/ml/hr. This value was four times higher than that by submerged culture.     

Immobilization of Lactobacillus rhamnosus in polyvinyl alcohol/calcium alginate matrix for production of lactic acid

Immobilization of Lactobacillus rhamnosus ATCC7469 in poly(vinyl alcohol)/calcium alginate (PVA/Ca-alginate) matrix using “freezing–thawing” technique for application in lactic acid (LA) fermentation was studied in this paper. PVA/Ca-alginate beads were made from sterile and non-sterile PVA and sodium alginate solutions. According to mechanical properties, the PVA/Ca-alginate beads expressed a strong elastic character. Obtained PVA/Ca-alginate beads were further applied in batch and repeated batch LA fermentations. Regarding cell viability, L. rhamnosus cells survived well rather sharp immobilization procedure and significant cell proliferation was observed in further fermentation studies achieving high cell viability (up to 10.7 log CFU g⁻¹) in sterile beads. In batch LA fermentation, the immobilized biocatalyst was superior to free cell fermentation system (by 37.1%), while the highest LA yield and volumetric productivity of 97.6% and 0.8 g L⁻¹ h⁻¹, respectively, were attained in repeated batch fermentation. During seven consecutive batch fermentations, the biocatalyst showed high mechanical and operational stability reaching an overall productivity of 0.78 g L⁻¹ h⁻¹. This study suggested that the “freezing–thawing” technique can be successfully used for immobilization of L. rhamnosus in PVA/Ca-alginate matrix without loss of either viability or LA fermentation capability.

     

Integration and expression of theEscherichia coli xylose isomerase gene inSchizosaccharomyces pombe

Summary The xyclose isomerase gene inEscherichia coli was cloned complementarily into a Leu2-negativeSchizosaccharomyces pombe mutant (ATCC 38399). The subsequent integration of the plasmid into the chromosomal DNA of the host yeast was verified by using the dot blot and southern blot techniques. The expressed xylose isomerase showed activity on a nondenaturing polyacrylamide gel. The expression of xylose isomerase gene was influenced by the concentration of nutrients in the fermentation broth. The yeast possessed a xylose isomerase activity of 20 nmol/min/mg by growing in an enriched medium containing yeast extract-malt extract-peptone (YMP) andd-xylose. The conversion ofd-xylose tod-xylulose catalyzed by xylose isomerase in the transformed yeast cells makes it possible to fermentd-xylose with ethanol as a major product. When the fermentation broth contained YMP and 5% (w/v)d-xylose, the maximal ethanol yield and productivity reached 0.42 g/g and 0.19 g/l/h, respectively.     

Enzyme specificity: “pseudopolymorphism” of lactate dehydrogenase in Drosophila melanogaster

An electrophoretic variant in the LDH (l-lactate:NAD oxidoreductase, E.C.1.1.1.27) of Drosophila melanogaster was observed on starch (or polyacrylamide) gels. This variant was found to exhibit an identical isozymic pattern (three isozymes with a decreasing staining density) on starch gel and map position as the Adh locus. On the other hand, anodal polyacrylamide gel electrophoresis in crude extracts has shown LDH to consist of nine bands and ADH of four bands. We have shown that ADH (Alcohol:NAD oxidoreductase, E.C.1.1.1.1) also oxidizes l(+)-lactate or d(–)-lactate with the NAD, while LDH oxidizes ethanol. By using various genetic and biochemical techniques, we have shown that the observed Ldh electrophoretic variant was not a real one and could be attributed to the presence of ADH. We have called this phenomenon pseudopolymorphism, and the problem of enzyme specificity has been examined. The appearance of a band in an assay using lactic acid as a substrate is not sufficient evidence for the presence of LDH. Hence, caution is called for before characterizing an electrophoretic band on a gel as being equivalent to the presence of a genetic locus. Out of the nine electrophoretic zones of activity observed on polyacrylamide gel (or out of the six previously observed) using crude extract, only two (one major and one minor) belong to LDH, as revealed by purified enzyme preparations. Furthermore, purified LDH exhibits activity in two bands on starch gel (out of three observed in crude extracts), which appear in different positions as compared with those of ADH. Finally, one band which responds to the presence of d(–)-lactate but not to l(+)-lactate has been revealed.     

Characterization of electrophoretically cryptic variation in the alpine butterfly Colias meadii

Enzyme polymorphism was characterized among the proteins of 14 loci of Coliae meadii by replicate electrophoresis in polyacrylamide gels of differing pore size. The results reveal a large number of variants, with a very skewed frequency distribution. A large fraction of the variants cannot be differentiated by electrophoresis in 5–7% acrylamide gels. This gel sieving approach permits an estimate of the relative contributions of charge and of conformation to electrophoretic mobility. Many of the variant proteins do not differ in charge. Most variants exhibit different degrees of interaction with the gel and presumably differ in conformation.This work was supported by grants from Washington University, the American Philosophical Society, the National Institutes of Health, and the National Science Foundation. Analysis was developed and carried out while the author was a Carnegie Institution of Washington Fellow.Carnegie Institution of Washington Department of Plant Biology Publication No. 569.     

Thermal Stability of Immobilized Glucoamylase Entrapped in Polyacrylamide Gels and Bound to SP-Sephadex C–50

Glucoamylase[α-1,4: 1,6-glucan-4: 6-glucohydroease, EC 3.2.1.3] from Rhizopus niveus was entrapped in polyacrylamide gels and adsorbed onto SP-Sephadex C–50 to elucidate the thermostability mechanism of immobilized enzymes. The thermal stability of immobilized glucoamylase entrapped in polyacrylamide gels was enhanced slightly compared with glucoamylase in free solution, and was independent of the acrylamide monomer concentration and N, N′-methylene-bis (acrylamide) content. To explain this phenomenon, the cellular structure of polyacrylamide gel was taken into consideration in addition to interactions between glucoamylase and gel, and a decrease in dielectric constant in the gel [S. Moriyama et al., Agric. Biol. Chem., 41, 1985 (1977)¹⁾]. On the other hand, immobilized glucoamylase bound to SP-Sephadex by ionic interaction showed lower stability than free glucoamylase, and much greater stability than glucoamylase in the presence of dextran sulfate, a constituent of SP-Sephadex. Thermal stabilities for the free and immobilized enzymes were also compared at the pH not in the bulk solution, but in the SP-Sephadex.     

A comparative electrophoretic study of the seed albumins fromSophora microphylla andPisum sativum (Leguminosae)

The albumin proteins from seed ofSophora microphylla Ait. and from cotyledons ofPisum sativum L. (cv. Greenfeast) have been analysed electrophoretically using a range of gels of varied pore size. Plots of mobility [as 100 log₁₀ (R _f × 100)] vs.acrylamide content of gel indicate that very few of the albumins fromS. microphylla are homologous with albumins fromP. sativum. Despite the diverse compositions of the two fractions, their amino acid analyses were surprisingly similar.     

Biosorption of Chromium,Cadmium, and Cobalt from Aqueous Solution by Immobilized Living Cells of Chryseomonas luteola TEM 05

Abstract

In this work, the potential use of the immobilized cells of Chryseomonas luteola TEM 05 for the removal of Cr⁺⁶, Cd⁺² and Co⁺² ions from aqueous solutions was investigated. The living cells of C. luteola TEM 05 were firstly entrapped both in carrageenan and chitosan coated carrageenan gels and then used in biosoption of the metal ions in batch reactors at pH 6.0, 25°C, in 100 mg L^?1 of each metal solution. Besides this, a process of competitive biosorption of these metal ions was also described and compared to single metal ion adsorption in solution. According to the immobilization results, the replacement of KCl by KCl-chitosan as gelling agent improved the mechanical strength and thermal stability of the gel. In addition, the C. luteola TEM 05 immobilized carrageenan-chitosan gel system was quite more efficient for the fast adsorption of metal ions from aqueous solution than the carrageenan gels without biomass.