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.     

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)     

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.     

高速逆流色谱技术在生物大分子分离纯化中的应用

高速逆流色谱是一种连续液-液色谱技术,具有无固相载体、样品无需严格预处理等优点。近10年来,在设备结构和溶剂体系等方面进行了大量的研究开发,已推广应用于生物技术、医药、天然产物、环境监测、食品等领域。为适应生物大分子和活性细胞的分离,采用条件温和的双水相体系,研究开发相应的高速逆流色谱设备已成为热点。针对双水相体系的特点,已经开发出了多种具有较高固定相保留率的新型高速逆流色谱设备,通过优化实验条件,成功地进行了多种蛋白质的分离纯化。本对该领域的最新进展进行了综述与评价。     

混合碳源发酵生产头孢菌素C过程优化

本文对头孢菌素C（Cephalosporin C,CPC）发酵过程中碳源补料控制策略进行了优化研究,提出了一种基于DO—Stat的混合碳源流加策略,提高了发酵整体性能。在7L发酵罐上对使用该策略和传统补油策略的头孢菌素发酵性能进行比较,结果表明,采用补加混合碳源（葡萄糖＋豆油）策略时,CPC终浓度最高,达到36．99g／L,CPC得率也从使用传统单纯补油策略时的11．39％提高到22．19％,代谢副产物去乙酰氧头孢菌素C（DAOC）的积累量少,DAOC／CPC只有0．38％,达到生产要求。     

Expression of cefF significantly decreased deacetoxycephalosporin C formation during cephalosporin C production in Acremonium chrysogenum

Deacetoxycephalosporin C (DAOC) is not only the precursor but also one of the by-products during cephalosporin C (CPC) biosynthesis. One enzyme (DAOC/DAC synthase) is responsible for the two-step conversion of penicillin N into deacetylcephalosporin C (DAC) in Acremonium chrysogenum, while two enzymes (DAOC synthase and DAOC hydroxylase) were involved in this reaction in Streptomyces clavuligerus and Amycolatopsis lactamdurans (Nocardia lactamdurans). In this study, the DAOC hydroxylase gene cefF was cloned from Streptomyces clavuligerus and introduced into Acremonium chrysogenum through Agrobacterium tumefaciens-mediated transformation. When cefF was expressed under the promoter of pcbC, the ratio of DAOC/CPC in the fermentation broth significantly decreased. These results suggested that introduction of cefF could function quite well in Acremonium chrysogenum and successfully reduce the content of DAOC in the CPC fermentation broth. This work offered a practical way to improve the CPC purification and reduce its production cost.     

The improvement of cephalosporin C production by fed-batch culture ofCephalosporium acremonium M25 using rice oil

The objective of this study is to improve cephalosporin C (CPC) production by optimization of medium and culture conditions. A statistical method was introduced to optimize the main culture medium. The main medium for CPC production was optimized using a statistical method. Glucose and corn steep liquor (CSL) were found to be the most effective factors for CPC production. Glucose and CSL were optimized to 2.84 and 6.68%, respectively. CPC production was improved 50% by feeding of 5% rice oil at day 3rd and 5th day during the shake flask culture ofC. acremonium M25. The effect of agitation speeds on CPC production in a 2.5-L bioreactor was also investigated with fed-batch mode. The maximum cell mass (54.5 g/L) was obtained at 600 rpm. However, the maximum CPC production (0.98 g/L) was obtained at 500 rpm. At this condition, the maximum CPC production was improved about 132% compared to the result with batch flask culture.     

Magnetic aqueous two-phase separation in preparative applications.

Magnetic aqueous two-phase separation is a new technique to speed up the separation of aqueous two-phase systems (Anal. Biochem. 1987, 167, 331-339). It is based on the addition of magnetically susceptible material (e.g. 1-micron iron oxide particles) which induces rapid phase separation when a mixed system is placed in a magnetic field. The technique has been applied to a number of two-phase systems. The time for phase separation was decreased by a factor of 5-240,000, with the largest improvement for systems containing high concentrations of protein and for systems with viscous or nearly isopycnic phases. An apparatus for preparative multistage extraction with magnetic separation was constructed and tested on glycolytic enzymes present in a yeast extract using a dextran/Cibacron blue-polyethylene glycol system. The presence of iron oxide particles did not adversely affect the extracted enzymes. An electromagnet-based apparatus for continuous phase separation on a larger scale was also designed. A phase system containing crude dextran and unpurified cell homogenate was effectively processed. The apparatus also allowed effective separation when the phase containing iron oxide particles was only a small fraction (4%) of the total phase system.     

高速逆流色谱法从白芍中分离纯化五没食子酰基葡萄糖

本文建立高速逆流色谱(HSCCC)方法,从白芍粗提物中分离纯化五没食子酰基葡萄糖.分别采用正己烷-乙酸乙酯-甲醇-水体积比0.5∶5∶1∶5及0.5∶5∶0.5∶5混合溶剂作为两相溶剂体系,上相为固定相,下相为流动相,转速为800 rpm,流速为2.0 mL/min,用HPLC检测及ESI-MS进行验证.经过两次HSCCC分离纯化,得到五没食子酰基葡萄糖纯度为95.7％.     

Two-step immobilized enzyme conversion of cephalosporin C to 7-aminocephalosporanic acid

The first large-scale production of 7-aminocephalosporanic acid (7ACA) from cephalosporin C (CPC) using a wholly enzymatic synthesis method is reported here. We produced 7ACA from CPC in as high a molar yield as 85% using the immobilized enzymes D-amino acid oxidase (D-AOD) and glutaryl-7-ACA acylase (GL-acylase). In the first reactor, CPC is converted to keto-adipyl-7-aminocephalosporanic acid (keto-7ACA) using an immobilized D-AOD isolated from a yeast, Trigonopsis variabilis. The keto-7ACA is then spontaneously converted to glutaryl-7-aminocephalosporanic acid (GL-7ACA) via a chemical reaction with hydrogen peroxide. The hydrogen peroxide is also a product of the D-AOD reaction. Near quantitative conversion of the keto-7ACA to GL-7ACA was observed. The second reactor converts GL-7ACA to 7ACA using an immobilized GL-acylase, which was isolated from a reconbinant Escherichia coli. The final 7ACA crystalline product is a high quality product. The reactions are conducted under very mild aqueous conditions: pH 8.0 and 20 degrees to 25 degrees C. The production of desacetyl side products is minimal. This process is currently being implemented on an industrial scale to produce 7ACA. (c) 1995 John Wiley & Sons, Inc.     

Deacylation activity of cephalosporin acylase to cephalosporin C is improved by changing the side-chain conformations of active-site residues

Semisynthetic cephalosporins are primarily synthesized from 7-aminocephalosporanic acid (7-ACA), mainly by environmentally toxic chemical deacylation of cephalosporin C (CPC). Thus, the enzymatic conversion of CPC to 7-ACA by cephalosporin acylase (CA) would be very interesting. However, CAs use glutaryl-7-ACA (GL-7-ACA) as a primary substrate and the enzymes have low turnover rates for CPC. The active-site residues of a CA were mutagenized to various residues to increase the deacylation activity of CPC, based on the active-site conformation of the CA structure. The aim was to generate sterically favored conformation of the active-site to accommodate the D-alpha-aminoadipyl moiety of CPC, the side-chain moiety that corresponds to the glutaryl moiety of GL-7-ACA. A triple mutant of the CA, Q50betaM/Y149alphaK/F177betaG, showed the greatest improvement of deacylation activity to CPC up to 790% of the wild-type. Our current study is an efficient method for improving the deacylation activity to CPC by employing the structure-based repetitive saturation mutagenesis.     

高速逆流色谱法分离制备丹酚酸B

采用高速逆流色谱法分离纯化丹参水溶性成分丹酚酸类物质,制备丹酚酸B化学对照品。分离采用的溶剂系统为正己烷-乙酸乙酯-水-甲醇(1.5:5:5:1.5),上相做固定相,下相做流动相,流速为1.7 mL/min,仪器转速850 rpm,进样量80 mg,纯度用HPLC方法测定。结果表明:一次分离可制备63.4 mg丹酚酸B,其纯度为98.6%。该方法操作简单,可作为高纯度丹酚酸B化学对照品的制备分离方法。     

Undefined xylose media extracted from biorefinery waste for enhanced and eco-friendly production of cephalosporin C by Acremonium chrysogenum M35

Xylose-rich undefined broth, extracted from the dilute acid pretreatment wastes of barley straw, serves as resourceful media for Acremonium chrysogenum M35 culture and production of cephalosporin C (CPC). Concentrating the extract with proper reprocessing enables to prepare various concentrations of xylose broth (2%–8%). The undefined xylose media were prepared for CPC production from A. chrysogenum M35 by the addition of other nutrients. Cell growth and CPC production were the most effective at 6% xylose and additional 2% glycerol, with maximum CPC production of 9.07 g/L after 6 days, which is higher production than that in defined media prepared with laboratory-level nutrients and reagents. Investigation of autotrophic and reverse trans-sulfuration pathways for cysteine synthesis, a limited element of three precursors for CPC synthesis, supports the enhanced CPC production in undefined media. Abundance of xylose ensures a maintained NADPH concentration required for sulfate reduction and synthesis of amino sulfide such as cysteine. Cystathionine-γ-lyase activity profiling indicated more efficient biosynthesis in undefined media than in other cultures use glycerol and glucose, and the biosynthesis pathway of CPC production by the cephalosporin gene cluster (i.e. pcbC and cefG genes) was investigated. The process using undefined xylose media was designed, and process simulation program confirmed our results.     

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     

Preparative isolation and purification of theaflavins and catechins by high-speed countercurrent chromatography

High-speed countercurrent chromatography (HSCCC) has been applied for the separation of theaflavins and catechins. The HSCCC run was carried out with a two-phase solvent system composed of hexane-ethyl acetate-methanol-water-acetic acid (1:5:1:5:0.25, v/v) by eluting the lower aqueous phase at 2 ml/min at 700 rpm. The results indicated that pure theaflavin, theaflavins-3-gallate, theaflavins-3'-gallate and theaflavin-3,3'-digallate could be obtained from crude theaflavins sample and black tea. The structures of the isolated compounds were positively confirmed by (1)H NMR and (13)C NMR, MS analysis, HPLC data and TLC data. Meanwhile, catechins including epigallocatechin gallate, gallocatechin gallate, epicatechin gallate and epigallocatechin were isolated from the aqueous extract of green tea by using the same solvent system. This study developed a modified method combined with enrichment theaflavins method by using HSCCC for separation of four individual theaflavins, especially for better separation of theaflavins monogallates.     

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.     

Novel polymer-polymer conjugates for recovery of lactic acid by aqueous two-phase extraction

A new family of polymer conjugates is proposed to overcome constraints in the applicability of aqueous two-phase systems for the recovery of lactic acid. Polyethylene glycol-polyethylenimine (PEI) conjugates and ethylene oxide propylene oxide-PEI (EOPO-PEI) conjugates were synthesized. Aqueous two-phase systems were generated when the conjugates were mixed with fractionated dextran or crude hydrolyzed starch. With 2% phosphate buffer in the systems, phase diagrams with critical points of 3.9% EOPO-PEI-3.8% dextran (DEX) and 3.5% EOPO-PEI-7.9% crude starch were obtained. The phase separation temperature of 10% EOPO-PEI solutions titrated with lactic acid to pH 6 was 35 degrees C at 5% phosphate, and increased linearly to 63 degrees C at 2% phosphate. Lactic acid partitioned to the top conjugate-rich phase of the new aqueous two-phase systems. In particular, the lactic acid partition coefficient was 2.1 in 10% EOPO-PEI-8% DEX systems containing 2% phosphate. In the same systems, the partitioning of the lactic acid bacterium, Lactococcus lactis subsp. lactis, was 0.45. The partitioning of propionic, succinic, and citric acids was also determined in the new aqueous two-phase systems.     

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.     

Preparative separation of helvolic acid from the endophytic fungus <Emphasis Type="Italic">Pichia guilliermondii</Emphasis> Ppf9 by high-speed counter-current chromatography

High-speed counter-current chromatography (HSCCC) was applied for preparative separation of helvolic acid from the crude extract of the endophytic fungus Pichia guilliermondii Ppf9, associated with the medicinal plant Paris polyphylla var. yunnanensis for the first time. The two-phase solvent system consisted of n-hexane-ethyl acetate-methanol-water (4.5:4.5:5.0:5.0, v/v) appending with phosphoric acid (0.2%, v/v) was employed. The revolution speed of the separation column, flow rate of the mobile phase and separation temperature of the apparatus were 800 rpm, 3 ml min(-1) and 25°C, respectively. About 6.8 mg of helvolic acid was successfully obtained from 450 mg of the crude extract by HSCCC within 4 h separation procedure, and its purity reached to 93.2% according to the HPLC analysis. The product was further characterized by MS, (1)H-NMR and (13)C-NMR spectra.     

Chromosomal polymorphism of Acremonium chrysogenum strains producing cephalosporin C

Using pulse electrophoresis in controlled homogenous electric field we performed molecular karyotyping of cephalosporin C-producing industrial and laboratory strains of Acremonium chrysogenum. Differences in size of several chromosomes of high-producing strain CB26/8 compared to the wild-type strain ATCC 11550 were revealed. It was shown that chromosomal polymorphism in the high-producing strain was not associated with alteration of localization and copy number of cephalosporin C (CPC) biosynthesis and transport genes. A cluster of ??early?? CPC biosynthesis genes is located on chromosome VI (4.4 Mb); a cluster of the ??late genes??, on chromosome II (2.3 Mb). Both clusters are presented as a single copy per A. chrysogenum genome in the wild-type and in CB26/8 high-producing strains. Based on comparative analysis of laboratory and industrial CPC producers, a karyotype scheme for A. chrysogenum strains of various origins was designed.