Production of l-glutamate by immobilized protoplasts

Summary Protoplasts of Brevibacterium flavum cultured in a medium containing 50 g·l^-1 of biotin were prepared with lysozyme and immobilized in matrices of agar-acetylcellulose filters. The immobilized protoplasts were applied to l-glutamate production from glucose and urea in a batch system. The productivity of l-glutamate by the immobilized protoplasts was 2.5 times higher than that by immobilized whole cells under optimal conditions. Maximal productivity initially reached 1.5 mg·ml^-1. The immobilized protoplasts of B. flavum could be used six times for l-glutamate production with retention of about 70% of the initial productivity.     

Characterization and optimization of a new immobilized system of κ-carrageenan through interaction with carob bean gum and polyols

The optimum relationships of κ-carrageenan and carob bean gum were investigated in order to obtain an immobilization system with better compression resistance, trapping capacity, and storage stability, and less syneresis phenomenon, when compared to κ-carrageenan itself. With that objective, different concentrations of polyols (glycerol and propylene glycol) were added, because of their water-retention characterization in the containing system. In this way, an improved system with good compression resistance was obtained: 15 × 10⁻⁴ N/m² in modified κ-carrageenan gel without E. coli cells and 11 × 10⁻⁴ N/m² with Escherichia coli cells. In the modified κ-carrageenan gel, the syneresis phenomenon decreased. The enzymatic activity in the system was 18 U/g, which did not present a change over a storage period of six months.     

Continuous production of l-phenylalanine from acetamidocinnamic acid using co-immobilized cells of Corynebacterium sp. and Paracoccus denitrificans

In order to produce l-phenylalanine efficiently from acetamidocinnamic acid with immobilized microbial cells, a two-step enzyme reaction using the acetamidocinnamate amidohydrolase activity of Corynebacterium sp. C-23 cells and the aminotransferase activity of Paracoccus denitrificans pFPr-1 cells was investigated. It was found that the useage of co-immobilized Corynebacterium sp. and P. denitrificans cells with κ-carrageenan was superior to that of the mixture of immobilized Corynebacterium sp. cells and immobilized P. denitrificans cells. When the space velocity was 0.06 h⁻¹ at 30°C, 147 mml-phenylalanine were produced with a 98% conversion ratio from acetamidocinnamic acid. The half-life of the l-phenylalanine-forming activity of the column was calculated to be ≈ 14 days at 30°C.     

Stability of fumarase activity of Brevibacterium flavum immobilized with ϰ-carrageenan and Chinese gallotannin

Summary In order to improve L-malic acid productivity by Brevibacterium flavum immobilized with -carrageenan, addition of Chinese gallotannin to the immobilization medium was investigated. As the results show, the optimal concentration of Chinese gallotannin was 0.1% (w/v). Fumarase activity and the stability of this improved preparation were higher than in one with only -carrageenan. Addition of Chinese gallotannin was more advantageous to stability towards ethanol than addition of polyethyleneimine. The L-malic acid productivity of the immobilized cells at 37°C was 42.2 kg/h per 1,000 l column, and increased threefold compared with that of B. flavum immobilized with only -carrageenan, and was 25 times that of B. ammoniagenes immobilized with polyacrylamide. Persimmon tannin also increased the stability of fumarase.     

Rifamycin B production by Nocardia mediterranei immobilized in a dual hollow fibre bioreactor

Continuous production of rifamycin B was studied using Nocardia mediterranei (ATCC 21789) immobilized in a dual hollow fibre bioreactor designed for cultivating aerobic cells. In the reactor operation the volumetric productivity based on the volume occupied by the immobilized cells was 108 mg l⁻¹ h⁻¹ when air was used for aeration and was 143 mg l⁻¹ h⁻¹ with pure oxygen. These corresponded to 22 and 30-fold increases over the productivity of the comparable batch system. These high productivities were due to the high cell mass density of 550 g l⁻¹. However, the specific productivity of the cell was 30–40% of that in the shake flask culture. As the residence time of medium in the reactor increased, pH of effluent rose to an alkaline region that was outside its optimum condition (pH 6.5–7.0) and the yield and productivity decreased.     

A Deuterium Effect in Insect Attraction

Brevibacterium flavum cells obtained from different growth phases were immobilized with κ-carrageenan and the stability of the fumarase activity was investigated. The stability of fumarase activity of the immobilized preparation of cells of the stationary growth phase was highest. The highest stability of the immobilized cells seemed to be correlated to the high stability of fumarase activity in free cells of the stationary phase. High rigidity of the cell wall and membrane of B. flavum cells of the stationary phase and firm binding of fumarase protein to the cell membrane were suggested from several lines of evidence obtained on treatment of the cells with lysozyme and detergents or sonication of the cells. Electronmicrographs showed that the cells of the stationary phase retained the original shape after repeated batch reactions. Solubilized fumarase prepared from cells of the stationary phase showed the highest stability. Experiments using the partially purified enzyme strongly suggested the existence of fumarase-stabilizing components in the cells.     

Screening of microorganisms having high fumarase activity and their immobilization with carrageenan

Summary To develop an efficient method for continuous production of L-malic acid from fumaric acid using immobilized microbial cells, screening of microorganisms having high fumarase activity was carried out and cultural conditions of selected microorganisms were investigated. As a result of screening microorganisms belonging to the genera Brevibacterium, Proteus, Pseudomonas, and Sarcina were found to produce fumarase in high levels. Among these microorganisms Brevibacterium ammoniagenes, B. flavum, Proteus vulgaris, and Pseudomonas fluorescens were further selected for their high fumarase levels in the cultivation on several media. These 4 microorganisms were entrapped into a k-carrageenan gel lattice, and the resultant immobilized B. flavum showed the highest fumarase activity and operational stability.Cultural conditions for the fumarase formation and the operational stability of fumarase activity of immobilized B. flavum are detailed. Productivity for L-malic acid using immobilized B. flavum with k-carrageenan was 2.3 fold of that using immobilized B. ammoniagenes with polyacrylamide.Presented at the Annual Meeting of the Agricultural Chemical Society of Japan, Nagoya, April 3, 1978     

Interactions between κ-carrageenan and chitosan in nanolayered coatings—Structural and transport properties

The interactions between κ-carrageenan and chitosan, two oppositely charged polysaccharides, have been investigated through microcalorimetric and quartz crystal microbalance measurements. Microcalorimetric measurements show that κ-carrageenan/chitosan interaction is an exothermic process and that the alternate deposition of κ-carrageenan and chitosan results in the formation of a nanolayered coating mainly due to the electrostatic interactions existing between the two polyelectrolytes (though other types of interactions may also be involved). Quartz crystal microbalance measurements confirmed that the alternating deposition of κ-carrageenan and chitosan resulted in the formation of a stable multilayer structure. The κ-carrageenan/chitosan nanolayered coating, assembled on a polyethylene terephthalate (PET) support, was characterized in terms of its surface (contact angle measurements) and gas barrier properties (water vapor and O₂ permeabilities) and analyzed by scanning electron microscopy (SEM). The water vapor permeability (WVP) and the oxygen permeability (O₂P) of the κ-carrageenan/chitosan nanolayers were found to be 0.020 ± 0.002 × 10⁻¹¹ and 0.043 ± 0.027 × 10⁻¹⁴ g m⁻¹ s⁻¹ Pa⁻¹, respectively. These results contribute to a better understanding of the type of interactions that play role during the construction of this type of nanostructures. This knowledge can be used in the establishment of an approach to produce edible, biodegradable multilayered nanostructures with improved mechanical and barrier properties for application in, e.g. food and biomedical industries.     

Continuous solvent production from whey permeate using cells of Clostridium acetobutylicum immobilized by adsorption onto bonechar

Cells of Clostridium acetobutylicum were immobilized by adsorption onto bonechar and used in a packed bed reactor for the continuous production of solvents from whey permeate. A maximum solvent productivity of 4.1 g l⁻¹ h⁻¹, representing a yield of 0.23 g solvent/g lactose utilized, was observed at a dilution rate of 1.0 h⁻¹. The reactor was operated under stable conditions for 61 days. High concentrations of lactose in the whey permeate favored solventogenesis, while low concentrations favored acidogenesis.     

Continuous production of L-malic acid by immobilized cells

l-Malic acid is used extensively in the pharmaceutical industry and as a food additive. It is now produced on an industrial scale by the enzymatic conversion of fumaric acid using immobilized cells of Brevibacterium flavum. Recent improvements to this system, especially the use of x-carrageenan supports, have resulted in a continuous process capable of yielding 30 tonnes of l-malic acid per month.     

Ethanol production by whole cell immobilization using lignocellulosic materials as solid matrix

Amongst four carriers used, rice-straw was found to be superior in terms of ethanol production. The maximum productivity (17.84 gl⁻¹ h⁻¹) corresponded to a dilution rate of 0.39 h⁻¹, the ethanol concentration being 45.80 gl⁻¹. A multistage rhomboidal bioreactor was found to partially overcome the disruption effect caused by the generation of a large volume of carbon dioxide in the column. Increases in productivity of about 12.55% and 3.6%, respectively, were achieved using rhomboidal and tapered bioreactors as compared to the cylindrical bioreactor. It was observed that the generation time of cells, in both the immobilized and free states, was around 2.5 h. The ethanol yield (Y_p/s) in the lower part of the reactor was less in comparison with other zones, where the substrate utilization efficiency was relatively higher.     

Entrapment of l-tryptophan producing Escherichia coli in different matrices: activity of immobilized cells

Cells of Escherichia coli induced for l-tryptophan synthase [l-serine hydro-lyase (adding indole-glycerol-phosphate), EC 4.2.1.20] have been assayed in DMF and DMSO aqueous solvents as reaction medium. Up to 20% DMF/water, cells retained 90% of their tryptophan synthase activity. Concentrations of 20 mM indole, which did not inhibit this reactivity, could be reached with 5% DMF/water. Four matrices were compared for cell immobilization: polyacrylamide, foam particles of bovine seum albumin, alginate and κ-carrageenan. The best activity was retained with the latter matrix, and the preparations thus obtained allowed high productivity of l-tryptophan. Various systems of production of l-tryptophan with κ-carrageenan and DMF/water were studied.     

Immobilization of Escherichia coli cells having aspartase activity with carrageenan and locust bean gum

Immobilization of Escherichia coli cells having aspartase activity was carried out by к-carrageenan, or by к-carrageenan and locust bean gum. To enhance operational stability, immobilized cells were treated with a hardening agent, such as glutaraldehyde or glutaraldehyde and hexamethylenediamine. Very active and stable immobilized preparations were obtained when E. coli cells immobilized with к-carrageenan were treated with 85 mm-glutaraldehyde and 85 mm-hexamethylenediamine. The productivities of E. coli cells immobilized with polyacrylamide, к-carrageenan, and к-carrageenan and locust bean gum were compared for production of $\text{l}\text{-}\text{aspartic}$ acid. Among these preparations, E. coli cells immobilized with к-carrageenan and treated with glutaraldehyde and hexamethylenediamine showed the highest productivity.     

Continuous production of acetic acid using immobilized acetobacter aceti in a three-phase fluidized bed bioreactor

Continuous operation of a three-phase fluidized bed bioreactor using immobilized cells showed that both immobilized and suspended cells contributed to the production of acetic acid. Unlike the rapid decrease in the productivity at dilution rates above 0.25 h⁻¹ in the free cell fermentation, the productivity was little affected by the dilution rate in the immobilized cell fermentation. Theoretical models were proposed for the continuous process. The models approximately agreed with the experimental results. Experimental results and/or theoretical calculations based on the kinetic models showed that suspended cells were important in the production of acetic acid if the solid holdup was small or if gel radius was large. Theoretical calculations showed that an optimal solid holdup or gel size existed at higher dilution rates because of the k_La dependence on solid holdup and particle diameter.     

Xylitol production in a bubble column bioreactor: Influence of the aeration rate and immobilized system concentration

This work evaluated the xylitol production from sugarcane bagasse hemicellulosic hydrolysate in a bubble column bioreactor using cells of the yeast Candida guilliermondii immobilized in calcium-alginate. The fermentation runs were performed according to a 2² full factorial design with three replicates at the center point in order to determine the effect of the variables: aeration rate (0.66–1.33 vvm) and immobilized system concentration (20–40% v/v), on the efficiency of xylose-to-xylitol conversion and on the xylitol volumetric productivity. The results indicated a significant influence of both variables on xylitol production. The highest conversion efficiency (41%) was attained using 1.33 vvm aeration rate and 40% immobilized system. Under these conditions, the volumetric productivity was 0.21 g l⁻¹ h⁻¹.     

Diffusion coefficients of carbohydrates in modified κ-carrageenan gels with and without Escherichia coli immobilized

Effective diffusion coefficients (Dag) of carbohydrates in modified κ-carrageenan gels, with and without Escherichia coli immobilized cells were determined. A diffusion cell based on the phenomena of sorption from a “well-stirred fluid” was used. Dag values were smaller in the gel with cells than without them. The effect of temperature on Dag was also studied.     

Production of thermophilic α-amylase using immobilized transformed Escherichia coli by addition of glycine

Efficient production of thermophilic α-amylase from Bacillus stearothermophilus was investigated using recombinant Escherichia coli HB101/pH1301 immobilized with κ-carrageenan by the addition of glycine. The effects of glycine, the concentrations of κ-carrageenan and KCI on the production of the enzyme as well as the stability of plasmid pHI301 were studied. In the absence of glycine, the enzyme was localized in the periplasmic space of the recombinant E. coli cells and a small amount of the enzyme was liberated in the culture broth. Although the addition of glycine was very effective for release of α-amylase from the periplasm of E. coli entrapped in gel beads, a majority of the enzyme accumulated in the gel matrix. (In this paper, production of the enzyme from recombinant cells to an ambient is expressed by the term “release”, while diffusion-out from gel beads is referred to by the term “liberate”.) Concentrations of KCI and immobilizing support significantly affected on the liberation of α-amylase to the culture broth. Mutants which produced smaller amounts of the enzyme emerged during a successive culture of recombinant E. coli, even under selective pressure, and they predominated in the later period of the passages. The population of plasmid-lost segregants increased with cultivation time. The stability of pHI301 for the free cells was increased by the addition of 2% KCI, which is a hardening agent for carrageenan. Although the viability of cells and α-amylase activity in the beads decreased with cultivation time during the successive culture of the immobilized recombinant E. coli, the plasmid stability was increased successfully by immobilization. Efficient long-term production of α-amylase was attained by an iterative re-activation-liberation procedure using the immobilized recombinant cells. Although the viable cell number, plasmid stability and enzyme activity liberated in the glycine solution decreased at an early period in the cultivation cycles, the process attained steady state regardless of the addition of an antibiotic.     

Continuous production of α-peptide using immobilized recombinant yeast cells: A model for continuous production of foreign peptide by recombinant yeast

α-Peptide, a portion of Escherichia coli β-galactosidase, was cloned downstream of the yeast α-factor promoter and the signal peptide by one of the authors. In this study, we utilized recombinant yeast cells, transformed the α-peptide secretion vector and attempted continuous production of α-peptide as a model of foreign peptide production. The continuous production of α-peptide was performed by using immobilized recombinant yeast cells on a column reactor, after characterizing the secretion, using minimal and complex medium. Utilizing minimal medium, with a productivity of 100 000 U h⁻¹ l⁻¹, α-peptide was continuously produced for more than 200 h. We then attempted to improve the productivity of α-peptide by alternating minimal and complex medium. Utilizing this medium changing method, 1.4 times higher α-peptide was produced during 150 h of operation compared with that achieved only by feeding minimal medium.     

Bioconversion of phenylpyruvic acid to l-phenylalanine by mixed-gel immobilization of Escherichia coli EP8-10

A mixed-gel of κ-carrageenan and gelatin was used in l-phenylalanine production. The mixed-gel, containing 87.5% κ-carrageenan and 12.5% gelatin [the total gel concentration was 4 wt%], showed the best performance and was selected for further study with Escherichia coli EP8-10. The optimum pH and temperature were 8.5 and 37 °C, respectively. The effects of trehalose and Mg²⁺ were studied in the mixed-gel immobilization. Their optimum concentrations were 5 × 10^?2 and 2 × 10^?3 mol/L, respectively. Under the optimal conditions, 98.3% of the phenylpyruvic acid (PPA) was converted to l-phenylalanine. The activity recovery of the transaminase enzyme in the mixed-gel immobilization was higher than that in single κ-carrageenan immobilization, which was 93.6%. The total PPA conversion rate was over 80% in all 15 batches, suggesting great sustainability in the mixed-gel immobilization. The maximum reaction rate (r_max) was calculated to be 4.75 × 10^?2 mol/(L g h).     

Continuous ethanol production from sago starch using immobilized amyloglucosidase and Zymomonas mobilis

To produce ethanol more economically than in a conventional process, it is necessary to attain high productivity and low production cost. To this end, a continuous ethanol production from sago starch using immobilized amylogucosidase (AMG) and Zymomonas mobilis cells was studied. Chitin was used for immobilization of AMG and Z. mobilis cells were immobilized in the form of sodium alginate beads. Ethanol was produced continuously in an simultaneous saccharification and ethanol fermentation (SSF) mode in a pacekd bed reactor. The maximum ethanol productivity based on the void volume, V_v, was 37 g/l/h with ethanol yield, Y_p/s, 0.43 g/g (84% of the theoretical ethanol yield) in this system. The steady-state concentration of ethanol (46 g/l could be maintained in a stable manner over two weeks at the dilution rate of 0.46 h⁻.