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     

Continuous production ofL-malic acid by immobilizedBrevibacterium ammoniagenes cells

Summary Continuous production ofL-malic acid from fumaric acid using immobilized microbial cells was investigated. Several microorganisms having fumarase activity were immobilized into a polyacrylamide gel lattice. Among the microorganisms tested, immobilizedBrevibacterium ammoniagenes IAM 1645 showed the highest enzyme activity, but produced an unwanted by-product, succinic acid. Conditions for suppression of this side reaction were investigated, and bile extract treatment of immobilized cells was found to be effective.The bile extract treatment of immobilized cells also resulted in a marked increase of reaction rate forL-malic acid formation.No difference was observed between the native enzyme and immobilized cells in optimal pH and temperature of the enzyme reaction.The effect of temperature on the reaction rate and the stability of fumarase activity of an immobilized cell column were investigated under conditions of continuous enzyme reaction. The decay of enzyme activity during continuous enzyme reaction was expressed by an exponential relationship. Half-life of the fumarase activity of the immobilized cell column at 37°C was calculated to be 52.5 days.Presented at the Annual Meeting of the Society of Fermentation Technology, Japan, Osaka, Japan, October 30, 1975.     

Immobilization of Brevibacterium flavum with carrageenan and its application for continuous production of l-malic acid

Extensive experiments were carried out to improve the productivity ofl-malic acid from fumaric acid using Brevibacterium flavum immobilized with carrageenan. The most favourable preparation for the continuous production ofl-malic acid was obtained when 16 g of B. flavum cells was entrapped in 100 ml 3.4% carrageenan gel. However, the immobilized cells produced an unwanted by-product, succinic acid. Treatment of the immobilized cells with 0.6% bile extract suppressed the side reaction and gave the highest operational stability of fumarase activity. By the immobilization of intact cells, the optimal temperature of the enzyme reaction shifted to 10°C higher, the optimal pH became broader, and the operational stability of fumarase activity increased. The effect of temperature on the stability of fumarase activity in the immobilized cell column was investigated under conditions of continuous enzyme reaction. The decay of fumarase activity during continuous enzyme reaction was expressed by an exponential relationship. The productivity of the immobilized B. flavum using carrageenan was as high as 5.2 times that of the conventional immobilized B. ammoniagenes using polyacrylamide.     

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.     

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.     

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.     

Colchicine-binding activity of carrot tubulin at different culture age

Tubulin contents in the extract from cultured carrot cells at different growth phases were investigated by measuring colchicine-binding activity. The addition of vinblastine and dithiothreitol to the reaction mixture appreciably improved the stability of both free and colchicine-bound tubulins. Colchicine-binding activity in the cell extract obtained from stationary phase was more labile than that from log phase though the extract showed higher affinity to colchicine. After purification, however, tubulin from the cells at different growth phases showed the same affinity and its colchicine-binding activity was much more stable than in crude extract. The colchicine-binding activity in the crude extract was corrected for the decay during measurement and apparent difference in the affinity so that the activity in the cells containing different kind and amount of interefering substances could be compared. The corrected amount of colchicine that binds to the 100,000×g extract was 46 pmol/10⁵ cells at log phase. It decreased with the progression of culture age from linear to stationary phase. Combining the data with the morphological observation, it was suggested that the log phase cells contained larger free tubulin pool than the linear or stationary phase cells.     

Inhibition of 5′-nucleotidase activity after growth of Dictyostelium discoideum

The specific activity of 5′-nucleotidase activity in cell-free extracts of Dictyostelium discoideum at both exponential and stationary growth phases was determined. The 5′-nucleotidase activity of both membrane and soluble fractions was determined. The results show that at exponential growth more activity is found in the soluble fraction. Furthermore, the results show that stationary phase cells contain about 10-fold less activity than cells at exponential growth. To determine if stationary phase cells contained an inhibitor of 5′-nucleotidase, purified membranes were incubated with a high speed supernatant (S-100) prepared from cells at this stage. The results showed not only a time and concentration dependent loss of membrane bound activity, but also that most of the lost activity could be recovered in a soluble form. This result suggested that the 5′-nucleotidase was being released by a factor in the S-100. Additional studies showed inactivation of the releasing factor by a protease and further, that this inactivation could be prevented by serine protease inhibitors. The specificity of releasing factor with respect to two other membrane bound activities was determined. The results indicated no loss of either 3′5′-cyclic phosphodiesterase or adenylate cyclase. In addition, the results of a comparison of the activity of the releasing factor at two stages of growth showed similar values at both exponential and stationary growth phase. This latter finding suggests that the loss of 5′-nucleotidase activity at stationary phase is not due to modulation of the releasing factor activity. An alternative mechanism is proposed.     

Growth kinetics of microalgae in microfluidic static droplet arrays

We investigated growth kinetics of microalgae, Chlorella vulgaris, in immobilized arrays of nanoliter‐scale microfluidic drops. These static drop arrays enabled simultaneous monitoring of growth of single as well as multiple cells encapsulated in individual droplets. To monitor the growth, individual drop volumes were kept nearly intact for more than a month by controlling the permeation of water in and out of the microfluidic device. The kinetic growth parameters were quantified by counting the increase in the number of cells in each drop over time. In addition to determining the kinetic parameters, the cell‐size distribution of the microalgae was correlated with different stages of the growth. The single‐cell growth kinetics of C. vulgaris showed significant heterogeneity. The specific growth rate ranged from 0.55 to 1.52 day^?1 for different single cells grown in the same microfluidic device. In comparison, the specific growth rate in bulk‐scale experiment was 1.12 day^?1. It was found that the average cell size changes significantly at different stages of the cell growth. The mean cell‐size increased from 5.99 ± 1.08 to 7.33 ± 1.3 µm from exponential to stationary growth phase. In particular, when multiple cells are grown in individual drops, we find that in the stationary growth phase, the cell size increases with the age of cell suggesting enhanced accumulation of fatty acids in older cells. Biotechnol. Bioeng. 2012; 109: 2987–2996. © 2012 Wiley Periodicals, Inc.     

l-Malic Acid Fermentation by Mixed Culture of Rhizopus arrhizus and Proteus vulgaris

When Rhizopus arrhizus NRRL 1526 was mix-cultured with Proteus vulgaris AHU 1144, a strain having a high fumarase activity, in a medium containing glucose as a substrate, fumaric acid fermentation was successively converted to l-malic acid fermentation and large amounts of l-malic acid were accumulated as an end product.

As an inoculum of P. vulgaris for this fermentation, cells in the stationary growth phase (48 to 72 hr culture) were much more favorable than those in the exponential growth phase (18 hr culture) and malic acid yields in the former case were as high as about 70 to 75 % based on initial glucose after 3 to 4 days of the mixed culture.     

Immobilization of Brevibacterium flavum cells on collagen for the production of glutamic acid in a recycle reactor

In this study, live cells of Brevibacterium flavum were immobilized for the production of glutamic acid. The reason for such a choice was that glutamic acid fermentation is an extensively studied fermentation and one which requires the viability of entire cellular faculties for the acid production. Brevibacterium flavum was chosen because it is an industrially used bacterium, and is very potent via a vis glutamic acid production. Studies were performed to find aeration and agitation conditions for optimal growth and glutamic acid productivity. Experiments were also done to find the optimum harvesting time. The cell activity peaks during the run of fermentation, and the time at which the peak occurs, was found. Conventional methods for immobilizing the cells on collagen were found to be lacking. The pH and drying were the two main reasons for loss of viability of the cells; the latter being more important. A modified immobilization procedure has been devised, which can immobilize live cells at any given pH and ionic strength, in contrast to the conventional method which requires the pH to be above 11 or below 3. This new method involves dialysis of collagen in suitable dialysis bags against water at pH7 (or buffer at any desired pH). The dialysed collagen blended at 20,000 rpm, resulted in a very smooth dispersion, unnoticeably different from collagen dispersion prepared at pH 11. The dispersed collagen was then cast and dried at an elevated temperature, and high air flow rate over the cast membrane, decreasing the time of drying from 6–8 hr ( in the conventional method) to 1.5–2 hr. The membrane has been tested for glutamic acid producing capabilities in a column reactor with the membrane spirally wound. The reactor has been operated under continuous conditions for 5–10 days with stable activities.     

Glyceraldehyde-3-phosphate dehydrogenase,a glycolytic enzyme present in the periplasm of Aeromonas hydrophila

This is the first report describing the glycolytic enzyme, glyceraldehyde-3-phosphate dehydrogenase (GAPDH), as a protein associated with the cell envelope of a gram-negative bacterium (Aeromonas hydrophila). Dose-dependent GAPDH activity was detected in whole bacterial cells from exponentially growing cultures, indicating that an active form of GAPDH is located outside the plasma membrane. This activity represents roughly 10–20% of total cell activity, and it is not reduced by pretreatment of the cells with trypsin. Assays with soluble GAPDH indicate that the activity measured in intact cells does not originate by rebinding to intact cells of cytosolic enzyme released following cell lysis. GAPDH activity levels detected in intact cells varied during the growth phase. The relationship between GAPDH activity and cell culture density was not linear, showing this activity as a major peak in the late-logarithmic phase (A₆₀₀ = 1.1–1.3), and a decrease when cells entered the stationary phase. The late exponential growing cells showed a GAPDH activity 3 to 4-fold higher than early growing or stationary cells. No activity was detected in culture supernatants. Enzymatic and Western-immunoblotting analysis of subcellular fractions (cytosol, whole and outer membranes, and periplasm) showed that GAPDH is located in the cytosol, as expected, and also in the periplasm. These results place the periplasmic GAPDH of A. hydrophila into the family of multifunctional microbial cell wall-associated GAPDHs which retain their catalytic activity. This revised version was published online in June 2006 with corrections to the Cover Date.     

Biosynthesis of γ-aminobutyric acid (GABA) using immobilized whole cells of <Emphasis Type="Italic">Lactobacillus brevis</Emphasis>

On an industrial scale, the production of γ-aminobutyric acid (GABA) from the cheaper sodium L-glutamate (L-MSG) is a valuable process. By entrapping Lactobacillus brevis cells with higher glutamate decarboxylase (GAD) activity into Ca-alginate gel beads, the biotransformation conditions of L-MSG to GABA were optimized with the immobilized cells. The cells obtained from a 60-h culture broth showed the highest biotransformation efficiency from L-MSG to GABA. The optimal cell density in gel beads, reaction pH and temperature were 11.2 g dry cell weight (DCW) l⁻¹, 4.4 and 40°C respectively. The thermal stability of immobilized cells was significantly higher than free cells. Under the optimized reaction conditions, the yield of GABA reached above 90% during the initial five batches and the yield still remained 56% in the tenth batch. Continuous production of GABA was realized with a higher yield by incorporating cell re-cultivation using the packed bed reactor.     

Characterization of a Cell Membrane-Associated Proteinase from Lactobacillus helveticus CRL 581

The production of a proteinase from Lactobacillus helveticus CRL 581 was studied. The highest specific activity was found at the early exponential growth phase of cells cultured in milk. The lowest levels of proteinase were detected in MRS broth, while in the casein–yeast extract–glucose broth enzyme production increased gradually during the fermentation and reached maximal values at the stationary phase. The proteinase, found to be associated with the cell membrane fraction, hydrolyzed β-casein more rapidly than α-casein. The enzyme was not released from washed cells in the presence or absence of calcium, which suggests that the enzyme did not undergo self-digestion. Received: 28 January 1997 / Accepted: 8 March 1997     

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.     

Production of L-malate from fumarate by the yeast Dipodascus magnusii

An alternative microbiological method for the production of malate from fumarate is presented. The yeast Dipodascus magnusii was used for this bioconversion. The optimum cell growth temperature was 28°C and the working volume 120 ml. The highest level of fumarase activity during bioconversion was achieved at a pH of 7.5 and a temperature of 37°C. These conditions were determined as optimal. Using sodium fumarate (1M), the maximum specific productivity of malic acid obtained was 1.72 g/(g_DCW × h) for intact cells. In the case of ammonium fumarate, it was 2.25 g/(g_DCW × h).     

Lectin-binding glycoconjugates in Paramecium primaurelia: changes with cellular age and starvation

 Lectins with different sugar specificities and binding to phagosome-lysosome systems as well as cell surface constituents were used to study glycoconjugate variation throughout culture and clonal life in Paramecium primaurelia, particularly during the transition period from logarithmic to stationary growth phase and in relation to clonal decline, respectively. These lectins include Griffonia simplicifolia agglutinin II (GS II), Ricinus communis agglutinin (RCA₁₂₀), Arachis hypogea agglutinin (PNA), succinyl concanavalin A (succinyl-con A), and Triticum vulgaris agglutinin (WGA). The labeling obtained varies both according to the lectin used and to the culture and clonal age of the cells. Negative results were obtained in logarithmic growth phase cells and in clonal young cells by using lectin GS II. Conversely, lectins RCA₁₂₀ and PNA bind to the cell surface, the oral region as well as cilia, and do not undergo modifications with culture or clonal age and after permeabilization. WGA binds to constituents of the cell surface, trichocyst tips, food vacuoles, the oral region, and cilia but the extent of labeling decreases as culture age increases; during clonal decline, cells show the same labeling pattern as starved cells. Finally, the lectin succinyl-con A shows a large amount of binding sites on the cell surface, on trichocyst tips, and in the oral region of logarithmic-phase cells, whereas the number of sites decreases in late stationary phase. The data obtained partly differ from those reported in the literature and the differences can be attributed to the culture conditions and species examined. Nevertheless, the assumption that a rearrangement of some glycoconjugates of membrane throughout culture and clonal life of Paramecium is confirmed. Accepted: 25 November 1996     

Effects of nitrogen starvation on the photosynthetic physiology of a tropical marine microalga Rhodomonas sp. (Cryptophyceae)

The effects of nitrogen starvation on biomass composition and photosynthetic function were examined in the marine cryptophyte Rhodomonas sp. Batch-cultured cells in N-sufficient medium showed a 2.5-fold increase in total carbohydrate content, and a 33% increase in cell volume when the cultures reached the stationary growth phase. These cultures also increased the ratio of phycoerythrin (PE)/hydrosoluble proteins from 6 to 22% by the 4th and 10th day of culture, respectively. In contrast, light-saturated photosynthetic activity (P_m) progressively decreased, and the value obtained at the beginning of the stationary phase was about 45% of that obtained for cells in the late exponential growth phase. Transfer to N-lacking medium caused a 3.2-fold increase in cell volume. N starvation also triggered a rapid decline in N-containing compounds such as hydrosoluble proteins and photosynthetic pigments, causing an almost complete loss of PE. The ratio of PE/hydrosoluble proteins decreased from 6 to 1% after 6 d of N deprivation. Furthermore, the PSII fluorescence capacity declined under N-starved conditions, which caused a pronounced decrease in both the P_m (circa 90%) and the apparent photosynthetic efficiency (circa 55%). Under these conditions, photosynthetically fixed carbon was used to synthesize large amounts of carbohydrates. We suggest that, in addition to the role of phycoerythrin as a light-harvesting pigment, Rhodomonas sp. responds to N-depleted conditions by mobilizing combined nitrogen from biliproteins.     

Physiological aspects of surface-immobilized Catharanthus roseus cells

Summary Growth and alkaloid production of surface-immobilized C. roseus cells were studied in a 2-1 bioreactor. Media designed to maximize cell growth or alkaloid production were employed. Nitrate and carbohydrate consumption rates as well as growth rates and biomass yields of immobilized cultures were equal or somewhat lower than for cell suspension cultures. Respiration rate (O₂ consumption and CO₂ production rates) of immobilized C. roseus cell cultures was obtained by on-line analysis of inlet and outlet gas composition using a mass spectrometer. Respiration rate increased during the growth phase and decreased once the nitrogen or the carbon source was depleted from the medium. The respiration rate of immobilized C. roseus cells resembled rates reported in the literature for suspension cultures. Offprint requests to: Denis Rho     

High expression of a human lactoferrin in transgenic tobacco cell cultures

Transgenic Nicotiana tabacum cell lines were developed expressing the human lactoferrin gene driven by the oxidative stress-inducible peroxidase (SWPA2) promoter. Western blot analysis showed the accumulation of both the full-length human lactoferrin protein as well as a immuno-reactive truncated fragment. Accumulation of human lactoferrin as monitored by ELISA increased proportionally to cell growth and reached a maximal (up to 4.3% of total soluble proteins) at the stationary phase of growth. Protein extracts from transgenic tobacco cells exhibited antibacterial activity.