Production of cephalosporin C in a fluidized-bed bioreactor

Production of cephalosporin C was investigated in a fluidized-bed bioreactor using bioparticles of Cephalosporium acremonium. Bioparticles were developed by forming a biofilm of growing hyphae around celite particles which contained spores of the microorganism. Production of the antibiotic was significantly improved by using bioparticles over the free mycelial culture, possibly due to the enhanced mass transfer capacity of the bioreactor system and successive generation of highly productive morphological forms of the microorganism. The maximum attainable titer of cephalosporin C from the bioreactor system was almost double that from a jar fermentor operation with a free mycelial culture of the same strain. The biofilm of the bioparticles became unstable as the fermentation proceeded. Morphological differentiation of the microorganism caused a gradual loss of biofilm and an increase of free cells in the culture broth. Additional feeding of a limited amount of methionine to the fermentation broth was not as effective as expected for improving the bioparticle stability. However, repeated use of the bioparticles revealed a strong possibility to improved the overall reactor performance since it allowed an enhanced production of the antibiotic with fewer free cells.     

Defining an optimal carbon source/methionine feed strategy for growth and cephalosporin C formation by Cephalosporium acremonium.

The effect of the method of methionine addition, growth-limiting carbon source (glucose vs sucrose), and culture growth rate on cephalosporin C production was investigated in a Cephalosporium acremonium defined medium fed batch fermentation. Batch addition of methionine, at a concentration of 3 g/L, prior to the start of a fed sucrose fermentation was found to interfere with the ability of the culture to utilize this sugar, thus limiting growth and decreasing cephalosporin C production. Batch methionine addition had no effect on glucose-limited cultures. Concurrent exponential feeding of methionine with sucrose improved both culture growth and productivity. Under the control of identical carbon source limiting feed profiles, sucrose was observed to support greater cephalosporin C production than glucose. Optimal cephalosporin C production in a C. acremonium defined medium fed batch fermentation was obtained through controlling culture growth during the rapid growth phase at a relatively low level with respect to mumax (mu approximately 0.036 h-1) until achieving a desired cell mass with a concurrent sucrose and methionine feed, followed by maintaining relatively vigorous growth (mu approximately 0.01 h-1) with sucrose for the duration of the fermentation.     

Formation of Desacetylcephalosporin C in Cephalosporin C Fermentation

The origin of desacetylcephalosporin C in cephalosporin C fermentation broths was investigated. Esterase activity was detected in cell-free extracts of Cephalosporium acremonium, but these extracts failed to deesterify cephalosporin C. When cephalosporin C was added to sterile and inoculated fermentation media, the antibiotic decayed at nearly identical rates. The formation of desacetylcephalosporin C during the fermentation was measured by quantitative chromatography and by the incorporation of valine-1-(14)C into the molecule. The rate constants obtained from the results of these experiments were equivalent to those for the decay of cephalosporin C in sterile and inoculated media. The data demonstrate that desacetylcephalosporin C is produced by nonenzymatic hydrolysis of cephalosporin C.     

Separation of cephalosporin C and desacetyl cephalosporin C by high speed counter-current chromatography in aqueous two-phase systems

Summary In the recovery of cephalosporin C (CPC) from fermentation broth, the separation of desacetyl cephalosporin C (DAC) is a major concern. Multistage extraction in aqueous two-phase systems, mainly PEG/ammonium sulfate systems, proved to be promising. In preparative scale operation, high speed counter-current chromatography (HSCCC) with eccentric columns was used with aqueous two-phase systems to obtain baseline resolution of CPC and DAC. Solvents (e.g. 5% acetone) or neutral salts (e.g. 1.45% KSCN) added into aqueous two-phase systems enhanced the separation efficiency. Operation parameters of HSCCC such as rotational speed and mobile phase flow rate can affect the retention of the stationary phase and HETP.     

Factors affecting cephalosporin C biosynthesis

Summary Caprolactam, butan-2-one, butan-2-ol, and butan-1, 3-diol were found to have a stimulating effect on the biosynthesis of cephalosporin C by a mutant strain ofCephalosporium. Caprolactam was shown to have a synergistic effect, when added to the fermentation medium together with each of the other three compounds.     

Genetic engineering approach to reduce undesirable by-products in cephalosporin C fermentation

Deacetoxycephalosporin C (DAOC) is produced by Acremonium chrysogenum as an intermediate compound in the cephalosporin C biosynthetic pathway, and is present in small quantities in cephalosporin C fermentation broth. This compound forms an undesirable impurity, 7-aminodeacetoxycephalosporanic acid (7-ADCA), when the cephalosporin C is converted chemically or enzymatically to 7-aminocephalosporanic acid (7-ACA). In the cephalosporin C biosynthetic pathway of A. chrysogenum, the bifunctional expandase/hydroxylase enzyme catalyzes the conversion of penicillin N to DAOC and subsequently deacetylcephalosporin C (DAC). By genetically engineering strains for increased copy number of the expandase/hydroxylase gene, we were able to reduce the level of DAOC present in the fermentation broth to 50% of the control. CHEF gel electrophoresis and Southern analysis of DNA from two of the transformants revealed that one copy of the transforming plasmid had integrated into chromosome VIII (ie a heterologous site from the host expandase/hydroxylase gene situated on chromosome II). Northern analysis indicated that the amount of transcribed expandase/hydroxylase mRNA in one of the transformants is increased approximately two-fold over that in the untransformed host. Received 5 January 1998/ Accepted in revised form 29 May 1998     

Expression of a cephalosporin C esterase gene in <Emphasis Type="Italic">Acremonium chrysogenum</Emphasis> for the direct production of deacetylcephalosporin C

A recombinant fungal microorganism capable of producing deacetylcephalosporin C was constructed by transforming a cephalosporin C esterase gene from Rhodosporidium toruloides into Acremonium chrysogenum. The cephalosporin C esterase gene can be expressed from its endogenous R. toruloides promoter or from the Aspergillus nidulans trpC promoter under standard Acremonium chrysogenum fermentation conditions. The expression of an active cephalosporin C esterase enzyme in A. chrysogenum results in the conversion of cephalosporin C to deacetylcephalosporin C in vivo, a novel fermentation process for the production of deacetylcephalosporin C. The stability of deacetylcephalosporin C in the fermentation broth results in a 40% increase in the cephalosporin nucleus.     

Extraction of cephalosporin C from whole broth and separation of desacetyl cephalosporin C by aqueous two-phase partition

Cephalosporin C was extracted from diluted or whole broth by PEG/salt aqueous two-phase systems. Parameters such as PEG molecular weight, salt type, pH, and salt concentration were investigated for finding a suitable extraction system. In PEG 600/ammonium sulfate or phosphate systems, K(c) (partition coefficienct of cephalosporin C) was observed to be larger than 1, with K(d) (partition coefficient of desacetyl cephalosporin C) being smaller than 1. The particular values of these coefficients would imply that the difficult separation of cephalosporin C and desacetyl cephalosporin C could possibly be achieved via the aqueous two-phase extraction. The addition of surfactants, water-miscible solvents, and neutral salts for enhancement of the separation efficiency was also investigated. The addition of surfactants to the system did not affect the separation efficiency substantially. K(c) would increase whereas K(d) decreased as a result of the addition of acetone, MeOH, EtOH, IPA, and n-BuOH. Meanwhile both K(c) and K(d) would decrease whenever neutral salts, NaCl, KCl, Kl, or KSCN, were added. The partitioning behavior of cephalosporin C and desacetyl cephalosporin C in filtered, whole, and different batches of broth was notably quite similar to that of diluted broth. The recovery yield of cephalosporin C in whole broth extraction was observed to be a function of centrifugal force used in phase separation. (c) 1994 John Wiley & Sons, Inc.     

Fatty acids reduce the tensile strength of fungal hyphae during cephalosporin C production in Acremonium chrysogenum

Fragmentation rate constants, which can be used to estimate the tensile strength of fungal hyphae, were used to elucidate relationships between morphological changes and addition of fatty acids during cephalosporin C production in Acremonium chrysogenum M35. The number of arthrospores increased gradually during fermentation, and, in particular, was higher in the presence of rice oil, oleic acid or linoleic acid than in their absence. Because supplementation of rice oil or fatty acids increased cephalosporin C, we concluded that differentiation to arthrospores is related to cephalosporin C production. To estimate the relative tensile strengths of fungal hyphae, fragmentation rate constants (k _frag) were measured. When rice oil, oleic acid, or linoleic acid were added into medium, fragmentation rate constants were higher than for the control, and hyphal tensile strengths reduced. The relative tensile strength of fungal hyphae, however was not constant presumably due to differences in physiological state.     

Ammonium repression of cephalosporin production by Streptomyces clavuligerus

Production of beta-lactam antibiotics took place during growth of Streptomyces clavulgerus in chemically defined medium. The specific activities of isopenicillin N synthetase ("cyclase"), isopenicillin N epimerase, and deacetoxycephalosporin C synthetase ("expandase") increased during the exponential phase of growth. Specific cephalosporin productivity during fermentation followed a similar pattern, reaching a maximum near the end of the growth phase and decaying rapidly in the stationary phase. Ammonium chloride depressed cephalosporin production, presumably as a result of repression of cyclase and expandase formation, but not of epimerase. No inhibitory effects on enzyme activity by ammonium were found. Addition of tribasic magnesium phosphate [Mg3(PO4)2 X 8H2O] prevented the repression of cyclase and markedly stimulated cephalosporin production. Cephamycin C and, in smaller amounts, O-carbamoyldeacetylcephalosporin C were the only cephalosporins detected. Growth with ammonium resulted in lower titers of both compounds, and did not change the relative proportion of each. The correlation found between cephalosporin productivity and cyclase specific activity in different media suggests that formation of this enzyme may be the rate-limiting step in the pathway.     

Fusion protein of Vitreoscilla hemoglobin with D-amino acid oxidase enhances activity and stability of biocatalyst in the bioconversion process of cephalosporin C

In this study we constructed an artificial flavohemoprotein by fusing Vitreoscilla hemoglobin (VHb) with D-amino acid oxidase (DAO) of Rhodotorula gracilis to determine whether bacterial hemoglobin can be used as an oxygen donor to immobilized flavoenzyme. This chimeric enzyme significantly enhanced DAO activity and stability in the bioconversion process of cephalosporin C. In a 200-mL bioreactor, the catalytic efficiency of immobilized VHb-DAO against cephalosporin C was 12.5-fold higher than that of immobilized DAO, and the operational stability of the immobilized VHb-DAO was approximately threefold better than that of the immobilized DAO. In the scaled-up bioprocess with a 5-L bioreactor, immobilized VHb-DAO (2500 U/L) resulted in 99% bioconversion of 120 mM cephalosporin C within 60 min at an oxygen flow rate of 0.2 (v/v) x min. Ninety percent of the initial activity of immobilized VHb-DAO could be maintained at up to 50 cycles of the enzymatic reaction without exogenous addition of H(2)O(2) and flavin adenine dinucleotide (FAD). The purity of the final product, glutaryl-7-aminocephalosporanic acid, was confirmed to be 99.77% by high-performance liquid chromatography (HPLC) analysis. Relative specificity of immobilized VHb-DAO on D-alpha-aminoadipic acid, a precursor in cephalosporin C biosynthesis, increased twofold, compared with that of immobilized DAO, suggesting that conformational modification of the VHb-DAO fusion protein may be altered in favor of cephalosporin C.     

A cephalosporin C acetylhydrolase is present in the cultures of Nocardia lactamdurans

Two protein bands with strong esterase activity are present in broths of Nocardia lactamdurans MA4213 cultures. One of them shows cephalosporin C acetylhydrolase (CAH) activity. This activity is maximal at 48 h of growth and shows a pattern of regulation slightly different from that of cephamycin production in medium supplemented with glucose (166 mM), glycerol (326 mM) or ammonium chloride (60 mM). The CAH activity was purified to homogeneity by DEAE-Sepharose ion-exchange, Sephadex G-75 gel filtration, and phenyl-Sepharose hydrophobic interaction chromatography. It showed a molecular mass of 72,100 Da. The N-terminus of the protein was determined and showed the amino acid sequence GGAAPGGPGAHPLWLPAGKD. The enzyme showed K _m values of 7.0 mM and 8.3 mM for cephalosporin C and 7-aminocephalosporanic acid respectively but was not active on cephamycin C. Received: 17 December 1999 / Received revision: 22 February 2000 / Accepted: 25 February 2000     

Methionine control of cephalosporin C formation

DL -Norleucine, a nonsulfur analogue of methionine was found to markedly stimulate synthesis of cephalosporin C by Cephalosporium acremonium strain CW19 in three different chemically defined media. Methionine, but not norleucine, stimulated cephalosporin C biosynthesis in a crude medium. The lack of stimulation by norleucine in complex medium was shown to be due to lack of uptake of this amino acid by mycelia growing in such a medium. In defined media containing a suboptimal methionine concentration, norleucine stimulated antibiotic production up to the level reached by optimal methionine. At an optimal dose of methionine, norleucine elicited no further increase in cephalosporin C production, indicating that these two amino acids act by the same mechanism. The data strongly indicate that stimulation by methionine is not a function of its ability to donate sulfur for antibiotic formation. Methionine was found to neither repress nor inhibit cysteine metabolism.     

Production of cephalosporin C,and its intermediates,by raised-titre strains of Acremonium chrysogenum

Three different strains of Acremonium chrysogenum have been grown under identical fermentation conditions and their profiles with respect to cephalosporin C and its intermediates were compared. Clear differences were found between the strains; one notably accumulated a large pool of penicillin N, showing a reduced ability to convert this antibiotic to the later intermediates in the pathway, deacetoxycephalosporin C, deacetylcephalosporin C and cephalosporin C.     

Constant dissolved oxygen concentrations in cephalosporin C fermentation: Applicability of different controllers and effect on fermentation parameters

Summary The behaviour and applicability of several controllers for maintaining a constant dissolved oxygen concentration (DO) during the cephalosporin C production with Cephalosporium acremonium in a laboratory fermentor is described. The process controllers were realized on a MC 68000 based process computer using the real-time language PEARL. The discrete signum integral controller showed the best control action. In addition some derived fermentation data were calculated on-line by the process computer.The results obtained by comparison of fermentations carried out at DO between 10% and 40% saturation during ideophase indicate that high DO leads to a high specific production rate for cephalosporin C and a low specific production rate for penicillin N and vice versa. In the range of DO investigated the production of deacetyl and deacetoxy cephalosporin C is not affected by DO. A direct correlation between DO and the yield coefficients Y _P/S and Y _P/X could be established. The yield coefficient Y _P/O for cephalosporin C is constant in the DO range from 10%–40%.Dedicated to Prof. Dr. H. J. Rehm on the occasion of his 60th birthday     

头孢菌素C生物合成调控研究进展北大核心CSCD

头孢菌素C由丝状真菌顶头孢霉产生,属于β-内酰胺类抗生素。其经改造后的7-氨基头孢烷酸是头孢类抗生素的重要中间体。头孢类抗生素在国内外抗生素市场中占有巨大的份额,是临床上的主要抗感染药物。随着分子生物学的发展,头孢菌素C的生物合成途径已基本阐明。为提高头孢菌素C的产量和降低生产成本,越来越多的研究者开始关注其较为精细、复杂的调控机制。本文重点对头孢菌素C生物合成及其调控机制的最新进展进行了简述,希望为今后头孢菌素C生产菌株的菌种改造和传统产业的升级换代提供一定的借鉴。     

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.     

Influence of dissolved oxygen concentration on the biosynthesis of cephalosporin C.

Cephalosporin C was produced by a highly productive strain of Cephalosporium acremonium under industrial production conditions by fed-batch cultivation in a 40-l stirred-tank reactor using a complex medium containing 50 g l-1 peanut flour. The influence of dissolved oxygen concentration (pO2, DOC), which was maintained at different constant levels between 5 and 40% of its saturation value, during the production phase by means of a parameter-adaptive pO2-controller, on the cephalosporin C biosynthesis, was investigated. The concentrations of cephalosporin C (CPC) and its precursors penicillin N (PEN N), deacetoxycephalosporin C (DAOC), and deacetylcephalosporin C (DAC) were monitored by 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 by off-line HPLC. By reducing the pO2 in the production phase from 40 to 5% of its saturation value, the CPC concentration diminished from 7.2 to 1.1 g l-1 and the PEN N concentration increased from 2.57 to 7.65 g l-1. The DAC concentration also dropped from 3.13 to 0.42 g l-1; however, the DAOC concentration was less influenced. The concentrations of AC and ACV were also less affected. The small DOC did not lead to an accumulation of the intermediate AC and ACV during the production phase. With increasing DOC in the range of 5-20%, the maximal specific production rate, the cell mass concentration-based and the substrate-based yield coefficients for CPC increased almost linearly, and fell back for PEN N.(ABSTRACT TRUNCATED AT 250 WORDS)     

Evolution of an acylase active on cephalosporin C

Semisynthetic cephalosporins are synthesized from 7-amino cephalosporanic acid, which is produced by chemical deacylation or by a two-step enzymatic process of the natural antibiotic cephalosporin C. The known acylases take glutaryl-7-amino cephalosporanic acid as a primary substrate, and their specificity and activity are too low for cephalosporin C. Starting from a known glutaryl-7-amino cephalosporanic acid acylase as the protein scaffold, an acylase gene optimized for expression in Escherichia coli and for molecular biology manipulations was designed. Subsequently we used error-prone PCR mutagenesis, a molecular modeling approach combined with site-saturation mutagenesis, and site-directed mutagenesis to produce enzymes with a cephalosporin C/glutaryl-7-amino cephalosporanic acid catalytic efficiency that was increased up to 100-fold, and with a significant and higher maximal activity on cephalosporin C as compared to glutaryl-7-amino cephalosporanic acid (e.g., 3.8 vs. 2.7 U/mg protein, respectively, for the A215Y-H296S-H309S mutant). Our data in a bioreactor indicate an ~90% conversion of cephalosporin C to 7-amino-cephalosporanic acid in a single deacylation step. The evolved acylase variants we produced are enzymes with a new substrate specificity, not found in nature, and represent a hallmark for industrial production of 7-amino cephalosporanic acid.