Citric acid production with alginate bead entrappedAspergillus niger ATCC 9142

Aspergillus niger ATCC 9142 mycelium was entrapped in calcium alginate beads and employed in an air-lift completely stirred reactor for continuous production of citric acid. Maximum yield obtained from 10% (w/v) sucrose was 12 g dm^-3 with about 40% fermentation efficiency. Maximum rate of production 70 mg g^-1 h^-1 was about five times that obtained in classical batch fermentation.     

Production of α-keto acids with alginate-entrapped whole cells of the yeastTrigonopsis variabilis

The yeast,Trigonopsis variabilis, was immobilized by entrapment in alginate. The immobilized cells containing high amounts of D-amino acid oxidase were used to convert D-amino acids to their corresponding α-keto acids.     

Application of magnetic immobilized microorganisms

Magnetic calcium alginate yeast beads, made by incorporation of magnetite or colloidal magnetic liquid, Ferrofluidℳ, exhibited catalytic behavior similar to that of their nonmagnetic counterparts. The magnetic immobilized preparations’ shortterm performance, long-term operational stability, and capacity forin situ activation were unaffected by the inclusion of magnetic material. The magnetic quality of the alginate beads provides manipulatory advantages.     

Immobilized cells in microbial nitrate reduction

The microorganismPseudomonas denitrificans was immobilized in alginate. These immobilized cells were capable of reducing 0.8 mg NO ₃ ^- /min/g wet weight of cells.     

Production of α-keto acids Part I. Immobilized cells ofTrigonopsis variabilis containing D-amino acid oxidase

Whole cells ofTrigonopsis variabilis were immobilized by entrapment in Ca²⁺-alginate and used for the production of α-keto acids from the corresponding D-amino acids. The D-amino acid oxidase within the immobilized cells has a broad substrate specificity. Hydrogen peroxide formed in the enzymatic reaction was efficiently hydrolyzed by manganese oxide co-immobilized with the cells. The amino acid oxidase activity was assayed with a new method based on reversed-phase HPLC. Oxygen requirements, bead size, concentration of cells in the beads, flow rate, and other factors were investigated in a “ trickle-bed ” reactor.     

Production of citric acid using immobilized conidia of Aspergillus niger

Conidia of Aspergillus niger were immobilized in calcium alginate gel for the production of citric acid. First, the type of the preactivation medium, together with the preactivation period, was investigated. It was found that A. niger requires a 2-d preactivation period at a 0.05 g/L NH₄NO₃ concentration. Second, preactivated cells were used to determine the effects of nitrogen concentration and the flow rate of oxygen and air on the production of citric acid. Maximum citric acid production was attained with medium containing 0.01 g/L of NH₄NO₃. The rate of citric acid production in the nitrogenous medium was 33% higher when oxygen was used instead of air during the production phase. This corresponds to an increase of 85% when compared to production when neither oxygen nor air was fed into the system. In the nonnitrogenous medium citric acid concentration remained similar regardless of the use of air or oxygen. However, in the nonnitrogenous production medium, citric acid production was not influenced considerably when oxygen was used instead of air. The advantage of using immobilized cells is that production is achieved easily in the continuous system. Therefore, citric acid production was also tested using a packed-bed bioreactor, and an increase in productivity by a factor of 22 was achieved compared to the batch system.     

Entrapment of living microbial cells in covalent polymeric networks

The kinetics of oxidative phenol degradation with microbial cellsCandida tropicalis, immobilized in a polyacrylamide and polymethacrylamide matrix, were mathematically simulated assuming zero-order and Michaelis-Menten rate equations. For zero-order kinetics an expanded equation for catalytic effectiveness as a function of the Thiele modulus, Biot number, and partition coefficients was derived and compared with numerical solutions for Michaelis-Menten kinetics. Errors with regard to the zero-order approximation become negligible ifc _o/K _M >2. Experimentally determined catalyst activities as a function of particle size and cell concentration were compared to calculated ones. Additional experiments to determine the diffusion and oxygen consumption ratios have been carried out in an effort to resolve the physical parameters to be used in the above mentioned calculations. Furthermore, experiments on cell growth during reincubation with nutrients and oxygen are reported; an increase in activity up to a factor of ten was observed. These experiments demonstrate that the microbial cells are entrapped in the polymer matrix in the living state.     

Studies on the overproduction of indole-containing metabolites by a methanol-utilizing yeast

Production of indole-containing metabolites (“indoles”) from methanol has been studied using a mutant ofHansenula polymorpha resistant to 5-fluorotryptophan. Whereas the wild-type culture produces only a small amount of indoles, the mutant is partially deregulated and overproduces indoles. Indoles production was studied in batch and continuous culture and in a washed-cell system. When the pH was above 4.0, indoles production was growth-associated, in both minimal and complex media, and batch or continuous culture. When the pH was below or equal to 4.0, a low phosphate concentration was found to improve production. In a phosphate-deficient washed-cell suspension system, the addition of an amino acid such as methionine at 5 mM increased specific productivity by more than 60%. Addition of cycloheximide at 50 mg/L decreased residual growth and increased maximum productivity of indoles by more than 60%. When the antibiotic was added at 1000 mg/L, growth was completely inhibited and indoles production continued for about 35 h.     

Continuous production of butanol with immobilized cells ofClostridium acetobutylicum

Spores ofClostridium acetobutylicum were immobilized in calcium alginate. An active gel preparation was obtained after outgrowth of the spores to vegetative cells within the gel matrix. A 100 mL column containing the immobilized cells was used for continuous production. At steady-state conditions the productivity of butanol was 67 g/L reactor volume/day.     

Production of propionic acid using a xylose utilizingPropionibacterium

The kinetics ofP. acidipropionici (ATCC25562), a xylose-utilizing rumen microorganism, was studied to assess its use for propionic acid production from wood hydrolyzates. Propionic acid has been shown to have a stronger inhibitory effect than acetic acid, with the undissociated acid form being responsible for the majority of the inhibitory effect. Thus, in batch tests with pH controlled at 6.0, the propionic acid concentration reaches 25 g/L and the acetic acid 7 g/L. Xylose uptake rate is dependent on the specific growth rate and glucose concentration. An immobilized cell columnar reactor at very high product yields (80%) proved adequate for propionic production. At cell concentrations of 95 g/L with high product concentration, volumetric productivities of 2.7 g/L·h were obtained in ultrafiltration cell recycle systems.     

Characteristics and production of thermostable α-amylase

Thermostable α-amylases have application in a variety of industrial processes and enzymes from a substantial number of thermophilic bacteria and fungi have been screened and characterized to varying degrees. The characteristics of these enzymes are summarized in this review. The genetics of α-amylase production inBacillus subtilis is reviewed and classical and recombinant DNA approaches to increasing α-amylase production are discussed.     

Denitrification and removal of heavy metals from waste water by immobilized microorganisms

Pseudomonas fluorescens, immobilized on soft polyvinyl chloride granules containing up to 35% softeners as carbon source, was used for simultaneous removal of nitrate and heavy metals. In typical continuous column operation, a 100 mg/L nitrate input solution was reduced to a 20 mg/L output at a feeding rate of 1500 mL/h, with a capacity of 14 kg/day/m³, and with an efficiency of 79%. In the same column, Pb(NO₃)₂ concentration was reduced from 1.0 to 0.05−0.1 mg/L and ZnSO₄ concentration was reduced from 10 to 5 mg/L.Pseudomonas aeruginosa immobilized on an O₂ plasma-treated melt blown polypropylene web was used for removing 95% of a 1.7 nCi PuCl₄ activity from a nuclear plant waste water in a batch operation.     

Reasons for the high stability of fumarase activity ofBrevibacterium flavum cells immobilized with k-carrageenan gel

Whole cells ofBrevibacterium flavum having high fumarase activity were immobilized using K-carrageenan. The reason for the high stability of fumarase activity of immobilized cells was investigated. One of main reasons for stabilizing fumarase activity by immobilization using K-carrageenan against organic solvents such as ethanol and acetone was the lower concentration of these solvents in the carrageenan gel compared with that in outer bulk solution. The stabilization of fumarase activity in the immobilized cells against protein-denaturing reagents was found to be related to rheological properties of K-carrageenan gel. Another reason for stabilizing fumarase activity by immobilization with K-carrageenan was to protect the cells from lysis. When immobilized cells were freeze-thawed, their fumarase activity increased and operation stability decreased. Therefore, one reason for the high decay of fumarase activity caused by the freeze-thawing may be a change in the pore size of the K-carrageenan gel. Fumarase activity and the operational stability of immobilized cells was found to depend on gelling conditions. Therefore, the steric structure of the K-carrageenan gel may be related to the decay of fumarase activity.     

Continuous production of L-aspartic acid

For the continuous production ofl-aspartic acid from fumaric acid and ammonia by the action of aspartase, the enzyme extracted fromEscherichia coli orE. coli cells having high aspartase activity were immobilized by various methods. In 1973 we succeeded in the industrial production ofl-aspartic acid usingE. coli cells immobilized with polyacrylamide gel. For the improvement of this process, we developed a novel technique using κ-carrageenan as the immobilizing matrix forE. coli cells. Further, EAPc-7 strain, having higher aspartase activity, was contracted from the parentE. coli by continuous cultivation with a definite medium. The aspartase activity was about seven times higher than that of the parent cells. In 1982 we changed from the conventional method to the improved method, using EAPc-7 strain immobilized with κ-carrageenan.     

Immobilization ofLactobacillus bulgaricus in a hollowfiber bioreactor for production of lactic acid from acid whey permeate

Lactobacillus bulgaricus was immobilized in the shell side of an industrial hollow-fiber ultrafiltration module. Acid whey permeate, containing 46 g/L lactose supplemented with 10 g/L yeast extract, was pumped through the tube side at dilution rates of 0.2–2.5/h. At a cell concentration of 100 g/L, productivity was 1.5–5 g lactic acid/L/h.     

The functional relationship between Baker’s yeast intracellular lysine and aeration rate and sodium chloride

The results of this study confirm the enhanced production of L-lysine bySaccharomyces cerevisiae during the fermentation of glucose at a 0.6M concentration of NaCl previously observed (8). Changes in NaCl concentration above or below 0.6M caused a drop in the maximum production of lysine. Fermentations run at 1.0, 1.4, and 1.8 VVM aeration rates and at 0.0, 0.3, 0.6, 0.9, and 1.2M NaCl concentrations gave the highest intracellular lysine yield at 0.6M and 1.4 VVM.     

Continuous production of lactic acid in a cell recycle reactor

The production of lactic acid from glucose has been demonstrated using a CSTR (continuous stirred-tank reactor) with cell recycle. Studies were conducted withLactobacillus delbrueckii at a fermentation temperature of 42°C and a pH of 6.25. A cell density of 140 g dry weight/L and a volumetric productivity of 150 g/L.h, with complete glucose consumption, were obtained. It was not possible to obtain a lactic acid concentration above 60 g/L because of product inhibition. A cell purge was not necessary to maintain high viability bacteria culture or to obtain a steady state. At steady state the net cell growth appeared to be negligible. The specific glucose consumption for cell maintenance was 0.33 g glucose/g cells-h.     

Industrial production of L-2-amino-4-phenylbutyric acid from 2-oxo-4-phenylbutyric acid by paracoccus denitrificans containing aminotransferase activity

An industrial production method of L-2-amino-4-phenylbutyric acid from 2-oxo-4-phenylbutyric acid by microbial cells containing aminotransferase activity was investigated. By usingParacoccus denitrificans pFPr-1, 0.19M L-2-amino-4-phenylbutyric acid was produced with a 95% conversion yield. Accumulated L-2-amino-4-phenylbutyric acid was readily isolated in pure form. Overall yield from 2-oxo-4-phenylbutyric acid was 83.7%.     

Tetraaryl-1,3-dioxolane-4,5-dimethanols as catalysts for the addition of trimethylsilyl cyanide to benzaldehyde and the oxirane ring

The synthesis of 1,2-, 1,3-, and 1,4-phenylene-bis[(4R,5R)-4,5-di(hydroxydiphenylmethyl)-1,3-dioxolane]s (ortho-, meta-, and para-bis-(R,R)-TADDOLs) and bis[4-{[(4R, 5R)-4,5-di(hydroxydiphenylmethyl)]-1,3-dioxolan-2-yl}phenyl]methane was carried out. The possibilities of the use of these compounds as catalysts for the C-C bond formation in the addition of Me₃SiCN to benzaldehyde and the oxirane ring opening in cyclohexene oxide by Me₃SiCN were investigated. The catalytic activity of different bis-(R, R)-TADDOLs in this series depends on their structure. Published in Russian in Izvestiya Akademii Nauk. Seriya Khimicheskaya, No. 8, pp. 1451–1458, August, 2007.     

Microencapsulation of astiban acid for the treatment ofSchistosomiasis mansoni

Schistosomiasis is among the top five diseases in the world in terms of morbidity, affecting perhaps 200 million people in tropical and subtropical countries. Antischistosomal drugs are toxic and rapidly metabolized. Hence, they must be given in a number of spaced doses. In spite of this there are severe side effects leading to poor patient compliance. This is an ideal situation for the application of sustained drug release to avoid the toxic peak concentration of drug. This study was carried out using Astiban acid, an antimonial drug that is effective againstS. mansoni. Unfortunately, the drug is sufficiently soluble that 50 mg will dissolve in 100 mL water in less than a minute. To permit sustained release of intramuscularly injected drug, microcapsules of astiban acid in poly(d,l-lactic acid) were formed by coacervation. Release studies show that an appreciable fraction of the drug is available at the surface for rapid solution. After this surface drug dissolves, the remaining drug is released slowly with half-times of many hours. After the initial burst, the release of drug follows Higuchi’s equation up to approximately 80% release, with exponentially decreasing release rates thereafter.