The role of valine in the biosynthesis of penicillin N and cephalosporin C by a Cephalosporium sp

1. The production of penicillin N, but not that of cephalosporin C, was inhibited by the addition of d-valine to suspensions in water of washed mycelium of Cephalosporium sp. 8650. The production of cephalosporin C was selectively inhibited by gamma-hydroxyvaline. 2. l-[(14)C]Valine was taken up rapidly and virtually completely by suspensions of washed mycelium but d-[(14)C]valine and alpha-oxo[(14)C]-isovalerate were taken up relatively slowly. 3. Part of the l-valine was rapidly degraded in the mycelium and part was incorporated into protein. Turnover of the valine in the amino acid pool was estimated to occur in 10-17min. 4. No detectable amount of l-[(14)C]valine was converted into the d-isomer in the mycelium. alpha-Oxo[(14)C]isovalerate was rapidly converted into l-[(14)C]valine in mycelium and mycelial extracts. 5. d-[(14)C]Valine was partially converted into the l-isomer in the mycelium and (14)C from d-valine was incorporated into protein. 6. The labelling of penicillin N and cephalosporin C by (14)C from l-[(14)C]valine was consistent with the view that l-valine is a direct precursor of C(5) fragments of both antibiotics and that any intermediates involved are present in relatively small pools in rapid turnover. 7. Labelling of the antibiotics with (14)C from d-[1-(14)C]valine appeared to occur after the latter had been converted into the l-isomer. Unlabelled d-valine did not decrease the efficiency of incorporation of (14)C from l-[1-(14)C]valine. 8. Intracellular peptide material which contained, among others, residues of alpha-aminoadipic acid, cysteine and valine, was rapidly labelled by (14)C from l-[1-(14)C]valine in a manner consistent with it being an intermediate in the biosynthesis of one or both of the antibiotics. 9. Labelling of penicillin N from l-[1-(14)C]valine occurred more rapidly than that of cephalosporin C. However, the effects of d-valine and gamma-hydroxyvaline on antibiotic production and the course of labelling of the antibiotics from l-[(14)C]valine could not readily be explained on the assumption that penicillin N was a precursor of cephalosporin C.     

Isolation and nature of intracellular peptides from a cephalosporin C-producing Cephalosporium sp

1. Three peptides containing alpha-aminoadipic acid and cysteine have been obtained in small amounts from the mycelium of a Cephalosporium sp. 2. The peptides were precipitated as cuprous mercaptides together with glutathione and resolved from the latter and from each other by preparative paper electrophoresis and chromatography either in the sulphonic acid form or as S-sulphonyl derivatives. From the S-sulphonyl derivatives they were obtained in the thiol form. 3. One peptide (P3) was shown by amino acid analysis and the mass spectrum of the NS-ethoxycarbonyl derivative of its methyl ester to be delta-(l-alpha-aminoadipyl)-l-cysteinyl-d-valine. A second peptide (P2) contained alpha-aminoadipic acid, cysteine, valine and glycine, and the third peptide (P1) contained alpha-aminoadipic acid, cysteine, beta-hydroxyvaline and glycine.     

Differential effect of cycloheximide on penicillin and cephalosporin biosynthesis by Cephalosporium acremonium

In resting cells of Cephalosporium acremonium CW19, protein synthesis was inhibited completely by 100 μg cycloheximide per ml. Furthermore, ongoing protein synthesis halted abruptly when cycloheximide was added after 20 min of incubation. Although cycloheximide did not affect the specific rate of penicillin N production, it markedly inhibited the specific rate of cephalosporin C production. The effect of cycloheximide was not influenced by the carbon source used to prepare the cells for the resting cell system.     

Influence of medium composition on the cephalosporin C production with a highly productive strain Cephalosporium acremonium.

Cephalosporin production by a highly productive Cephalosporium acremonium strain was carried out and optimized by fed-batch operation in a 40 l stirred tank reactor using a complex medium containing 30-120 g l-1 peanut flour. The concentrations of cephalosporin C (CPC) and its precursors: penicillin N (PEN N), deacetoxy cephalosporin C (DAOC), and deacetyl cephalosporin C (DAC) were monitored with an on-line HPLC. The concentrations of amino acids valine (VAL), cysteine (CYS), alpha-amino adipic acid (alpha-AAA), the dipeptide alpha-amino-adipyl-cysteine (AC), and the tripeptide alpha-amino-adipyl-cysteinyl-valine (ACV), were determined off-line by HPLC. The RNA content and dry weight of the sediment as well as the oxygen transfer rate (OTR) and the CO2 production rate (CPR) were used to calculate the cell mass concentration (X). The influences of peanut flour (PF) and the on-line monitored and controlled medium components: glucose (GLU), phosphate, methionine (MET) as well as the dissolved oxygen (DOC) on the cell growth, the product formation, and the pathway of cephalosporin C biosynthesis were investigated and evaluated. When the glucose fed-batch cycle was optimized and oxygen transfer limitation was avoided (DOC greater than 20% of the saturation value), high process performance (103.5 g l-1 X, 11.84 g l-1 CPC, a maximum CPC productivity of 118 mg l-1 h-1, and the whole concentration of the beta-lactam antibiotics CPC, DAC, DAOC, PEN N 17.34 g l-1) was achieved by using 100 g l-1 PF in the medium with the optimum concentration of phosphate (260-270 mg l-1) and a low glucose concentration (less than 0.5 g l-1). The cultivations with different medium concentrations demonstrated that the product formation was directly proportional to the cell mass concentration. On the average, the cell mass-based yield coefficient of CPC: YCPC/X amounted to 0.115 g CPC per g cell mass.     

Studies on the respiration rate of free and immobilized cells of Cephalosporium acremonium in cephalosporin C production

Bioprocesses using filamentous fungi immobilized in inert supports present many advantages when compared to conventional free cell processes. However, assessment of the real advantages of the unconventional process demands a rigorous study of the limitations to diffusional mass transfer of the reagents, especially concerning oxygen. In this work, a comparative study was carried out on the cephalosporin C production process in defined medium containing glucose and sucrose as main carbon and energy sources, by free and immobilized cells of Cephalosporium acremonium ATCC 48272 in calcium alginate gel beads containing alumina. The effective diffusivity of oxygen through the gel beads and the effectiveness factors related to the respiration rate of the microorganism were determined experimentally. By applying Monod kinetics, the respiration kinetics parameters were experimentally determined in independent experiments in a complete production medium. The effectiveness factor experimental values presented good agreement with the theoretical values of the approximated zero‐order effectiveness factor, considering the dead core model. Furthermore, experimental results obtained with immobilized cells in a 1.7‐L tower bioreactor were compared with those obtained in 5‐L conventional fermentor with free cells. It could be concluded that it is possible to attain rather high production rates working with relatively large diameter gel beads (ca. 2.5 mm) and sucrose consumption‐based productivity was remarkably higher with immobilized cells, i.e., 0.33 gCPC/kg sucrose/h against 0.24 gCPC/kg sucrose/h in the aerated stirred tank bioreactor process. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 63: 593–600, 1999.     

Cybernetic modeling of the cephalosporin C fermentation process by Cephalosporium acremonium

A cybernetic mathematical model has been developed to describe the production of cephalosporin C. In developing the model, diauxic behavior of substrate consumption, morphological differentiation of cells, and catabolite repression of cephalosporin C production by the preferred substrate, glucose, were considered. The proposed model was tested on the experimental data from the literature and could adequately describe the morphological differentiation of cells, the sequential utilization of carbon sources and the production of cephalosporin C. It could be a useful tool to optimize the production of cephalosporin C by Cephalosporium acremonium in batch, fed-batch or continuous operations.     

Synthesis of cephalosporin C by a methionine analogue resistant mutant of Cephalosporium acremonium

Summary DL-seleno-methionine resistant mutants of Cephalosporium acremonium were isolated which have an enhanced capacity to utilized sulfate for the synthesis of cephalosporin C. Of these mutants, one designated as SMR-I3 produced three-fold more cephalosporin C from sulfate than its parent CW19. Mutant SMR-I3 required less dl-methionine for maximal synthesis of cephalosporin C, but an excess of dl-methionine inhibited the synthesis of the antibiotic. Furthermore, the mutant accumulated excessive methionine in the amino acid pool and possessed superior activity for sulfate uptake. These observations indicate that in the mutant SMR-I3, the biosynthesis of methionine from sulfate is very active and excess methionine becomes available for the synthesis of cephalosporin C.     

Identification of rate-limiting steps in cephalosporin C biosynthesis in Cephalosporium acremonium: a theoretical analysis

Summary A kinetic model describing the biosynthesis of celphalosporin C in Cephalosporium acremonium has been developed to identify the rate-limiting step(s). Using this model and in-vitro kinetic data of the biosynthetic enzymes, the production kinetics of cephalosporin C were examined theoretically. The predicted time profile of the specific production rate during batch culture is in good agreement with that of experimental results published previously. Sensitivity analysis indicates that -(l--aminoadipyl)-l-cysteinyl-d-valine (ACV) synthetase is the rate-limiting enzyme. Our analysis also predicts that increasing ACV synthetase enhances the production rate initially until expandase/hydroxylase becomes rate-limiting. Furthermore, increasing expandase/hydroxylase reduces the accumulation of penicillin N, and thus, enhances the production of cephalosporin C. Based on our analysis, amplifying both ACV synthetase and expandase/hydroxylase concurrently should enhance the production rate to a great extent.Correspondence to: W. S. Hu     

Morphology and kinetics studies on cephalosporin C production by Cephalosporium acremonium M25 in a 30-l bioreactor using a mixture of inocula

AIMS: In this study, the relationship between morphology and cephalosporin C (CPC) production in a 30-l bioreactor culture of Cephalosporium acremonium M25 using a 3:7 seed mixture was investigated. In addition, the kinetic model was established and applied. METHODS AND RESULTS: CPC production was performed in a 30-l bioreactor using a 3:7 seed mixture. It was recognized that a 3:7 seed mixture was able to reduce lag phase and enhance CPC production. The maximum CPC production and cell mass were 1.96 and 81.5 g l-1 respectively. Through a morphology study by observation using image analysis, it was concluded that changes of morphological features predicted the progressive production of CPC and that a morphology study could be useful in monitoring the CPC fermentation by C. acremonium M25. In the kinetics study, a kinetic model of CPC fermentation was developed and applied. The proposed model could adequately describe the fermentation of C. acremonium M25 in a 30-l bioreactor. CONCLUSIONS: CPC productivity was improved by using a 3:7 seed mixture in a 30-1 bioreactor. The changes in morphological features showed a very similar tendency with CPC production. A kinetic model of CPC fermentation was successfully established. SIGNIFICANCE AND IMPACT OF THE STUDY: The results of the present study suggest that the use of a 3:7 seed mixture inocula has considerable possibilities for improving CPC productivity if applied to industrial scale fermentations. Through morphology and kinetics study, the kinetic model to describe the morphological differentiation and CPC production by C. acremonium M25 was established.     

Role of Acetyl CoA: Deacetylcephalosporin C Acetyltransferase in Cephalosporin C Biosynthesis by Cephalosporium acremonium

Existence of an acetyltransferase, which catalizes acetylation of deacetylcephalosporin C to cephalosporin C, was demonstrated for the first time in cell-free extracts of Cephalosporium acremonium. The pH optimum of the enzyme appeared to be 7.0 to 7.5 and the enzyme required essentially Mg²⁺ as a cofactor for its reaction. The activity of this enzyme was not observed in the cell-free extracts of deacetylcephalosporin C-producing mutants Nos. 20, 29, 36 and 40, but was recovered in a revertant obtained from the mutant No. 40. These results indicate that deacetylcephalosporin C accumulation by these mutants was due to the lack of the acetyltransferase and made it reasonable that the terminal reaction of cephalosporin C biosynthesis in Cephalosporium acremonium proceeded by the catalytic action of acetyltransferase.     

Biosynthesis of penicillin V acylase by Fusarium sp.: effect of culture conditions

Penicillin V acylase was produced, both intracellularly and extracellularly, by Fusarium sp. SKF 235 grown in submerged fermentation. When neopeptone was added to the medium, >95% of the penicillin V acylase was extracellular. In the absence of a complex organic nitrogen source, the fungus produced low levels of totally intracellular penicillin V acylase. MgSO₄ was essential for synthesis of the enzyme, which was induced by phenoxyacetic acid and penicillin V. The maximum yield of penicillin V acylase was 430 IU/g dry cell wt. The optimum pH value and temperature for the penicillin V acylase were 6.5 and 55°C, respectively.     

In vivo conversion of penicillin N into a cephalosporin type antibiotic by a non-producing mutant of Streptomyces clavuligerus

Summary Intact mycelia of beta-lactam antibiotic producing microorganisms are generally considered to be impermeable to externally fed penicillin. Using growing cells of the non-producing mutant. Streptomyces clavuligerus NP1, it was surprisingly possible to convert externally fed penicillin N into a cephalosporin type of antibiotic.Dedicated to Professor Dr. H. J. Rehm on the occasion of his 60th birthday.