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Both mycelial fragments and protoplasts were successfully employed for mutagenesis of Micromonospora rosaria NRRL 3718, and the results were compared. The optimal conditions and effective procedures for mutagenesis of M. rosaria by a chemical mutagen, N-methyl-N'-nitro-N-nitrosoguanidine, have been determined. Mutation was efficiently induced when mycelial fragments were treated with N-methyl-N'-nitro-N-nitrosoguanidine at a concentration of 0.3 to 0.5 mg/ml in the reaction buffer of pH 7.0. Optimal treatment time was 20 to 40 min. Ampicillin treatment was very effective for enrichment of auxotrophs. Protoplasts showed much higher sensitivity to the lethal effect of N-methyl-N'-nitro-N-nitrosoguanidine. Although protoplasts have some advantage of single cell characteristics, the frequency of auxotrophs obtained was somewhat lower. Up to 4% of the colonies were shown to be auxotrophs under the well-defined conditions. This mutagenesis method with protoplasts or fragmented mycelia (or both) should be applicable to other actinomycetes that have limited or no sporulation.

Auxotrophic strains of Micromonospora rosaria were isolated by N-methyl-N'-nitro-N'-nitrosoguanidine mutagenesis and used in intraspecific recombination by protoplast fusion. High-frequency fusion of protoplasts of M. rosaria strains was induced by polyethylene glycol (molecular weight, 1,000) (PEG 1,000). The optimum concentration of PEG 1,000 for fusion of M. rosaria was 50% (wt/vol). PEG 4,000 was slightly better than PEG 1,000 at concentrations lower than 50% (wt/vol). The recombinant frequency did not increase after treatment with PEG 1,000 (50% [wt/vol]) for longer than 20 min. Under these conditions, fusion with many auxotrophic strains of M. rosaria resulted in a high frequency of formation of true recombinants (sometimes more than 10%). Additionally, when ros (rosamicin nonproducing) strains were crossed by protoplast fusion; about 5% of the resultant prototrophic recombinants were shown to have the ros+ (rosamicin producing) characteristic restored. Rosamicin production by M. rosaria colonies was clearly distinguished by the broth overlay method. The results of fusion experiments between ros and ros+ strains indicated that either the chromosomal mutation or pleiotrophic effect of some auxotrophic markers is involved.

Some biochemical properties of whole-cell penicillin amidohydrolase from Micrococcus luteus have been studied. This whole-cell enzyme showed its maximal activity at 36 degrees C at pH 7.5. It was found that the activation energy of this enzyme was 8.03 kcal (ca. 33.6 kJ) per mol, and this amidohydrolase showed first-order decay at 36 degrees C. The penicillin amidohydrolase was deactivated rapidly at temperatures above 50 degrees C during storage or preincubation for 24 h. The Michaelis constant, Km, for penicillin G was determined as 2.26 mM, and the substrate inhibition constant, Kis, was 155 mM. The whole-cell penicillin amidohydrolase from M. luteus was capable of hydrolyzing penicillin G, penicillin V, ampicillin, and cephalexin, but not cephalosporin C and cloxacillin. This whole-cell enzyme also had synthetic activity for semisynthetic penicillins or cephalosporins from D-(--)-alpha-phenylglycine methyl ester and 6-alpha-aminopenicillanic acid or 7-amino-3-deacetoxycephalosporanic acid.

In order to develop a general methodology for evaluation of the gene expression efficiency for gene product, theoretical and experimental studies were undertaken using a recombinant Escherichia coli K12DeltaH1Deltatrp/ pPLc23trpA1 as a "gene-host cell" model system in a two-stage continuous-culture system. For this, a genetically structured kinetic model proposed earlier for biosynthesis of gene product in batch cultivation was extended to the two-stage continuous-culture system. A partial list of key parameters of the model includes the rate of plasmid segregation, specific growth rate of recombinant cell, plasmid content, rates of transcription and translation, and other parameters related to product biosynthesis. The dynamics of heterogeneous cell population containing plasmid-harboring and plasmid-free cells were also studied. Theoretical analysis of cell population dynamics shows that the recombinant cells could be maintained stably for a prolonged time in a two-stage continuous-culture system. Fermentation performance of the recombinant E. Coli cells in a two-stage continuous bioreactor system was examined experimentally, and the gene expression efficiency of a cloned gene product was determined based on the genetically structured kinetic model proposed. Based on our experimental results, the gene expression efficiency of the model gene-host cell system was found to be about twofold more efficient (i. e., 41.8 mg TrpA protein/mg plasmid DNA) as compared to the average rate of protein biosynthesis by E. coli cells. The performance of two-stage recombinant fermentation was also simulated using a mathematical model developed. General trends obtained from the model simulation agree reasonably well with the currently available experimental data, although further refinements need to be made. The methodology illustrated in this article could be used for evaluation of the gene expression efficiency of other genetically engineered recombinants once such recombinants with certain gene-host cell systems are constructed.

A new graphical method of determining the kinetic constants for immobilized-enzyme systems is proposed and illustrated with some examples. The advantages of using this method are that these kinetic constants can be determined accurately and conveniently from the conversion data of a packed-column enzyme-reactor system.

Two new penicillins and a new cephalosporin have been synthesized by condensing 2-hydroxy-1-naphthaldehyde with epicillin, 6-aminopenicillanic acid and cephradine, and subsequently reducing the SCHIFF bases with NaBH4. The antimicrobial activities of these compounds are also described.

The availability of a yeast strain which is capable of fermenting lactose and at the same time is tolerant to high concentrations of ethanol would be useful for the production of ethanol from lactose. Kluyveromyces fragilis is capable of fermenting lactose, but it is not as tolerant as Saccharomyces cerevisiae to high concentrations of ethanol. In this study, we have used the protoplast fusion technique to construct hybrids between auxotrophic strains of S. cerevisiae having high ethanol tolerance and an auxotrophic strain of lactose-fermenting K. fragilis isolated by ethyl methanesulfonate mutagenesis. The fusants obtained were prototrophic and capable of assimilating lactose and producing ethanol in excess of 13% (vol/vol). The complementation frequency of fusion was about 0.7%. Formation of fusants was confirmed by the increased amount of chromosomal DNA per cell. Fusants contained 8 x 10 to 16 x 10 mug of DNA per cell as compared with about 4 x 10 mug of DNA per cell for the parental strains, suggesting that multiple fusions had taken place.

A new combined bioreactor-separator system was designed and its operational feasibility demonstrated in order to develop a bioprocess that enables us to handle simultaneous biotransformation and recovery of product by crystallization. Enzymatic conversion of L-aspartate to L-alanine by L-aspartate beta-decarboxylase from Pseudomonas dacunhae (ATCC 21192) was used as a model system for this study to demonstrate the principles involved in the bioprocess design. Immobilized cells of P. dacunhae containing the enzyme were fluidized in a tapered column type of bioreactor and a filter-crystallizer combination was used as a separator unit in our experimental system.It was found that almost a theoretical yield was achieved, and the process control for both the bioreactor operation and separation was relatively easy. The Production systems, namely, the recirculating bioreactor separator combination system and the conventional batch reactor system, were analyzed and compared based on the results obtained form this study, and it was found that a significant cost reduction, by about 20%, can be achieved when the recirculating bioreactor-separator combination system was employed. Based on these findings, it is anticipated that the conceptual design of the bioreactor-separator combination system evaluated in this study has some potential for industrial application.

Rosamicin is one of the important macrolide antibiotics that has clinical efficacy and broad-spectrum antibacterial activity. Using a mutant strain of Micromonospora rosaria (NRRL 3718), a chemically defined medium was developed, and some fermentation conditions that are important to rosamicin biosynthesis were optimized to achieve rosamicin productivity of 230 mug/ml. Soluble starch and l-asparagine were found to be the best carbon and nitrogen sources, and a stimulative effect of magnesium and zinc ions was also found. The medium developed contains: soluble starch, 4%; l-asparagine, 0.15%; K(2)HPO(4), 0.075%; CaCO(3), 0.6%; MgSO(4) . 7H(2)O, 0.05%; FeSO(4) . 7H(2)O, 10 M; CuSO(4) . 5H(2)O, 10 M; ZnSO(4) . 7H(2)O, 10 M; and MnSO(4) . (4-6)H(2)O, 10 M. The required air supply was about 40 mmol of O(2) liter . h . atm, and the favorable culture temperature was 28 to 29 degrees C.

In the cellulase-cellulose reaction system, the adsorption of cellulase on the solid cellulose substrate was found to be one of the important parameters that govern the enzymatic hydrolysis rate of cellulose. The adsorption of cellulase usually parallels the rate of hydrolysis of cellulose. The affinity for cellulase varies depending on the structural properties of cellulose. Adsorption parameters such as the half-saturation constant, the maximum adsorption constant, and the distribution coefficient for both the cellulase and cellulsoe have been experimentally determined for several substrates. These adsorption parameters vary with the source of cellulose and the pretreatment methods and are correlated with the crystallinity and the specific surface area of cellulose substrates. The changing pattern of adsorption profile of cellulase during the hydrolysis reaction has also been elucidated. For practical utilization of cellulosic materials, the cellulose structural properties and their effects on cellulase adsorption, and the rate of hydrolysis must be taken into consideration.

Production of cellulase using solid culture systems of Trichoderma reesei QM9414 and Sporotrichum cellulophilum on wheat bran was studied. By using moisture-controlled solid culture equipment, the effect of water content of wheat bran on cell growth and cellulase production was investigated. Cellular biomass grown on solid substrate was estimated by measuring oxygen consumption rate and glucosamine content of the cells. These parameters were shown to have a good linear correlation with the specific growth rate. This reliable method of estimating the cell growth rate enabled us to simulate the enzyme production in a solid culture system by means of multiple linear regression analysis which takes into account of the water content, cell mass, and the oxygen consumption rate as variables. The cell growth and cellulase production were maximized at different water content of the medium. A high water content, 57% for T. reesei and 70% for S. cellulophilum, favored mycelial growth, while the maximum cellulase activity was obtained at a lower water content such as 50% for both fungi. It was observed that cellulase production by T. reesei depended on the culture conditions that support the optimal growth rate for the maximum enzyme production.

Eleven monoclonal antibodies against the cephalexin-synthesizing enzyme have been constructed and primarily characterized. These antibodies are all IgG1 type, with medium affinity, and with no enzyme-inhibition effect. They will be utilized as immunoadsorbents to purify their corresponding antigen, the enzyme, in one step.

Enzymatic synthesis of phenoxymethylpenicillin from 6-aminopenicillanic acid and phenoxyacetic acid methyl ester was attempted by using partially purified alpha-acylamino-beta-lactam acylhydrolase I (ALAHase I) enzyme from Erwinia aroideae NRRL B-138. The reaction rates were carefully followed by determination of 6-aminopenicillanic acid (6-APA), phenoxymethylpenicillin (PNV), phenoxyacetic acid (POA), phenoxyacetic acid methyl ester (POM), and phenoxyacetylglycine (POG) using high performance liquid chromatography. Among the acyl donors tested, POM gave the highest yield (12.2% based on 6-APA). The overall conversion increased almost linearly with an increase in molar ratio of POM to 6-APA up to 4:1. The effects of organic solvents on the overall yield were also evaluated. Some improvement of PNV yield was observed when ethanol, 2-propanol, and acetone were used. ALAHase I was found to carry out three reactions simultaneously: transfer of acyl group to acyl acceptor to form semisynthetic beta-lactam antibiotic; hydrolysis of acyl donor in amide or ester bond, and hydrolysis of semisynthetic beta-lactam antibiotic which was produced by the enzyme. It was also observed that the hydrolysis reactions of POM and PNV were irreversible in this reaction system. The optimal pH for the three reactions was different. They were: pH 9.0 for POM hydrolysis, 6.8 for the transfer of phenoxyacetyl group to 6-APA, and 6.0 for the PNV hydrolysis. The apparent Km values for POM, 6-APA and PNV were estimated as 33, 25 and 31 mM, respectively.

The changes in the cellulose structure by compression milling were studied and expressed in terms of crystallinity, accessibility, specific surface area, and degree of polymerization. The kinetic parameters, maximum reaction rate, and Michaelis constant were determined experimentally. Based on the experimental results a two-phase model, which is based on the degradation of cellulose by simultaneous actions of the cellulase complex on the crystalline and amorphous phases, is proposed. The relationships between cellulose accessibility and the kinetic parameters were compared with those predicted by the model. A good agreement was found, although the two-phase hypothesis is a simplification of the true state of order in cellulose.

The reaction kinetics of the enzymatic synthesis of cephalexin from 7-aminodeacetoxy cephalosporanic acid and phenylglycine methylester was studied using the synthesizing enzyme obtained from Xanthomonas citri. The activation energy, Km values for 7-aminodeacetoxy cephalosporanic acid and phenylglycine methylester, and Ki value for phenylglycine methylester were determined as 8.63 kcal/mol, 3.7mM, 14.5mM, and 70mM, respectively. The enzyme was found to be constitutive and susceptible to deactivation.

The importance of the consideration of micro-anatomical and cytological observation for the oxygen utilization by hybridoma cells are emphasized. Tumor cells have considerably lower content of mitochondria and that cells metabolize much of their carbon source by anaerobic pathway, therefore, consumes much less oxygen. Because of the fact that hybridoma cells are derived from a myeloma cell, which is a type of tumor cell, there may be possibility that the oxygen demand could be closely related to mitochondrial content of the resulting cell. Possible correlation between the optimum DOT and mitochondrial content of the hybridoma cells is hypothesized. By simulating oxygen transport inside of a single hybridoma cells for the cases of three different mitochondrial contents, possible differences in the optimum DOT according to the mitochondrial contents were studied and the results reported.

The relationship between butirosin biosynthesis and certain biochemical characteristics related to sporulation in a strain of Bacillus circulans NRRL B-3313 was examined. The cellular content of dipicolinic acid increased while the amount of poly-beta-hydroxybutyrate decreased with changes in antibiotic productivity. Oligosporogenous mutants failed to synthesize the antibiotic and to degrade poly-beta-hydroxybutyrate. These observations suggest that spore formation may be related to antibiotic production in this strain of B. circulans.

An improved synthesis of captopril using methacrylic acid as the starting material is described. Treatment of methacrylic acid (I) with a hydrogen halide gave the 3-halogeno-2-methylpropanoic acids II and III, which were treated with thionyl chloride to yield the corresponding 3-halogeno-2-methylpropanoyl chlorides IV and V. Treatment of IV or V with L-proline yielded the N-(R,S-3-halogeno-2-methylpropanoyl)-L-prolines VI and VII, which were separated into optically pure R- and S-diastereoisomers using dicyclohexylamine. Treatment of halides of VI or VII with methanolic ammonium hydrosulfide gave captopril in 28% yield.

For the purpose of saving the energy and raw materials required in glutamate fermentation, an immobilized whole-cell system was prepared and its performance in a continuous reactor system was evaluated. Corynebacterium glutamicum (a mutant strain of ATCC 13058) whole cell was immobilized in K-carrageenan matrix and the gel structure was strengthened by treatment with a hardening agent. The effective diffusivities of carrageenan gel for glucose and oxygen were found to decrease significantly with an increase in carrageenan concentration, while the gel strength showed an increasing trend. Based on the physical and chemical properties of carrageenan gel, the immobilization method was improved and the operation of the continuous reactor system was partially optimized. In an air-stirred fermentor, the continuous production of glutamate was carried out. The effect of the dilution rate on glutamate production and operational stability were investigated. The performance of the continuous whole-cell reactor system was evaluated by measuring glutamate productivity for a period of 30 days; it was found to be far superior to the performance of conventional batch reactor systems using free cells.

Derepression of the phage lambda p(L) promoter on recombinant plasmid pPLc 23-trpAl caused a rapid increase of plasmid free segregants in the population. In continuous culture, increased production of trpA protein follwing derepression was accompanied by a continuous deceleration of specific growth rate. In the repressed condition, plasmid loss per generation in continuous culture decreased as dilution rate increased from 0.06 to 1.08 h(-1). Over this range, the concentration of plasmid DNA within the cell decreased eightfold corresponding to a decrease in plasmid number from 74 to 32 molecules/cell. The use of a two-stage continuous culture system coupled with a temperature sensitive expression system allows a high trpA productivity from the derepressed plasmid for more than 48 h and also offers a possibility of minimizing the instability problem of high expression recombinants. Such a system also permits the critical study of the effects of fermentation and other regulatory parameters on expression under better controlled conditions than is possible in a batch culture or single-stage continous culture.

A tapered column type of bioreactor system packed with immobilized Saccharomyces cerevisiae was used to study the bioreactor performance as a function of design and operating variables. The performance of tapered column bioreactor system was found to be better than that of the conventional cylindrical column reactor system for the ethanol fermentation. The new bioreactor design alleviated problems associated with carbon dioxide evolution and provided a significantly better flow pattern for both liquid and gas phases in the bioreactor without local channelling. A mathematical simulation model, which takes into account of the axial convection and dispersion, interphase mass transfer, and apparent kinetic design parameters, was developed. The effect of radial concentration gradients on the bioreactor performance was found to be insignificant. For the reactor system studied, the maximum ethanol productivity obtained was 60 g ethanol/L gel/h, and the maximum glucose assimilation rate was 140 g glucose/L gel/h. One of the most important findings from this study was that the apparent kinetic parameters change at the glucose concentration of 2 g/L This change was found to be due to the changes in yeast physiology and metabolism. The values of V(m) (') and V(m) (') decreased from 0.8 to 0.39 g ethanol/g cell/h and from 97mM to 11mM, respectively. The substrate inhibition constant was estimated as 0.76M and the product inhibition constant was determined as 113 g ethanol/L The degree of product inhibition showed practically a linear relationship with an increasing ethanol concentration. Based on the hydro-dynamic analysis of the bioreactor system, it was found that the Peclet number, N(Pe) was not a strong function of the flow velocity at low flow rates through the bioreactor system, but its value decreased somewhat at an interstitial velocity greater than 0.03 cm/s. The tapered column bioreactor system showed a much better flow pattern of gas and liquid phases within the reactor, thereby providing a more homogeneous distribution of gas-liquid-solid phases in the reactor without any phase separation.

Microbial lipids produced by Rhodotorula gracilis NRRL Y-1091 grown in continuous culture under nitrogen-limiting condition were evaluated and the effects of growth rate and oxygen concentration on the degree of unsaturatoin of fatty acids studied. As the growth rate increased the protein content of the biomass increased but cell biomass, lipid content, and lipid productivity decreased; the specific lipid production rate remained constant at about 0.012 g lipid/g dry biomass/h. The maximum lipid content recorded was 49.8% (w/w) of the cell mass at a growth rate of 0.02 h(-1). The growth rate also affected fatty acid composition; polyunsaturated fatty acids (C18:2 and C18:3) increaded with growth rate while other fatty acids (C16:0, C18:0, C18:1) decreased. Increase in oxygen concentration between 5 and 234muM increased the lipid content without significantly affecting its degree of unsaturation. On the other hand, the degree of unsaturation was significantly affected by specific oxygen uptake rate for this obligate aerobe, Rh. gracilis.

In studying plasmid instability in recombinant microorganisms, Escherichia coli MV 12[p VH5] and MV 12 trpR[p VH5] harboring trp operon were used as experimental model systems. The host with the trp repression system was partially derepressed by 3-beta-indoleacrylic acid. The results from kinetic analysis of plasmid instability showed that the stability of p VH5 and the growth rate of MV 12[p VH5] decreased rapidly in presence of 3-beta-indoleacrylic acid at a concentration higher than 10 mug/mL, but beyond 30 g/mL no significant change was observed. This suggests that Trp(-) variants from MV 12[p VH5] could be produced from the host cells at a different frequency depending on the physiological condition. In another system, MV 12 trpR[p VH5] which was constructed by conjugation of E. coli MV 12[p VH5] with E. coli CSH61, the plasmid stability was much lower and the frequency of Trp(-) cell production was about 10 times higher as compared with the MV 12[p VH5] when treated with 3-beta-indoleacrylic acid. A kinetic model representing the plasmid instability was derived, and a fairly good agreement with the experimental results was found. The fraction of plasmid-free cell (or negative variant) shows a different time course profile depending on the segregation coefficient (a, production rate of negative variants from positive cells during one generation), growth ratio (G, the ratio of growth rates of negative variants to positive cells), and other parameters. The negative variant fraction continues to increase ("run away" type) or it approaches to a finite value ("settling" type) depending on the relative values of a and G.

For the purpose of improving ethanol productivity, the effect of air supplement on the performance of continuous ethanol fermentation system was studied. The effect of oxygen supplement on yeast concentration, cell yield, cell viability, extracellular ethanol concentration, ethanol yield, maintenance coefficient, specific rates of glucose assimilation, ethanol production, and ethanol productivity have been evaluated, using a high alcohol tolerant Saccharomyces cerevisiae STV89 strain and employing a continuous fermentor equipped with an accurate air metering system in the flow rate range 0-11 mL air/L/h. It was found that, when a small amount of oxygen up to about 80mu mol oxygen/L/h was supplied, the ethanol productivity was significantly enhanced as compared to the productivity of the culture without any air supplement. It was also found that the oxygen supplement improved cell viability considerably as well as the ethanol tolerance level of yeast. As the air supply rate was increased, from 0 to 11 mL air/L/h while maintaining a constant dilution rate at about 0.06 h(-1), the cell concentration increased from 2.3 to 8.2 g/L and the ethanol productivity increased from 1.7 to 4.1 g ethanol/L/h, although the specific ethanol production rate decreased slightly from 0.75 to 0.5 g ethanol/g cell/h. The ethanol yield was slightly improved also with an increase in air supply rate, from about 0.37 to 0.45 ethanol/g glucose. The maintenance coefficient increased by only a small amount with the air supplement. This kind of air supplement technique may very well prove to be of practical importance to a development of a highly productive ethanol fermentation process system especially as a combined system with a high density cell culture technique.

Some studies on the adsorption of cellulase on cellulose revealed part of the mechanisms involved in the enzymatic hydrolysis of cellulose and provided some clues to the synergistic mechanism of cellulase complex. The adsorption of cellulase was significantly affected by the reaction conditions and physical chemical characteristics of cellulose. Endoglucanase consisted of adsorbable and nonadsorbable components. Cellobiohydrolase had the strongest adsorption affinity. Each cellulase component is postulated to have distinctly different adsorption sites on cellulose, corresponding to the active sites in the hydrolysis reaction. Competitive adsorption kinetics between cellulase components were also observed during the adsorption process. The degree of competitive adsorption was most remarkable when the composition of cellulase components was nearly the same as that in the crude cellulase complex. This seems to show the optimal relative composition of cellulase components. The synergism between cellobiohydrolase and endoglucananse could be elucidated more clearly by this competitive adsorption model of the reaction mechanism.