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.     

Characteristic of immobilized cephalosporin C acylase and its application in one-step enzymatic conversion of cephalosporin C to 7-aminocephalosporanic acid

Cephalosporin C (CPC) acylase is an enzyme which hydrolyzes CPC to 7-aminocephalosporanic acid (7-ACA) directly, and therefore has great potential in industrial application. In this study, the CPC acylase from a recombinant Escherichia coli was purified to high purity by immobilized metal affinity chromatography, and the CPC acylase was covalently attached to three kinds of epoxy supports, BB-2, ES-V-1 and LX-1000EP. The immobilized CPC acylase with LX-1000EP as the support shows the highest activity (81 U g⁻¹) suggesting its potential in industrial 7-ACA production. The activity of immobilized enzyme was found to be optimal at pH between 8.5 and 9.5 and to increase with temperature elevation until 55 °C. Immobilized CPC acylase showed good stability at pH between 8.0 and 9.5 and at temperature up to 40 °C. To avoid product degradation, the production of 7-ACA utilizing immobilized enzyme was carried out at 25 °C, pH 8.5 in a designed reactor. Under optimal reaction conditions, a very high 7-ACA yield of 96.7% was obtained within 60 min. In the results of repeated batch production of 7-ACA, 50% activity of the initial cycle was maintained after being recycled 24 times and the average conversion rate of CPC reached 98%.     

Generation of a pH gradient in an immobilized enzyme system

Several examples of two-step sequential reactions exist where, because of the poor equilibrium conversion by the first reaction, it is desirable to conduct the two reactions simultaneously. In such a scheme, the product of the first reaction is continuously removed by the second reaction, thus not allowing the first reaction to approach chemical equilibrium. Therefore, the first reaction is allowed to proceed in the desired direction at an appreciable rate. However, in many biochemical applications where enzyme catalysts are involved, the enzyme's activities are strong functions of pH. Where the pH optima of the first and second reaction differ by three to four units, the above reaction scheme would be difficult to implement. In these cases, the two reactions can be separated by a thin permeable membrane across which the desired pH gradient is maintained. In this article, it was shown, both by theory and experiment, that a thin, flat membrane of immobilized urease can accomplish this goal when one face of the membrane is exposed to the acidic bulk solution (pH(b) = 4.5) containing a small quantity of urea (0.01 M). In this particular case, the ammonia that was produced in the membrane consumed the incoming hydrogen ions and thus maintained the desired pH gradient. Experimental results indicate that with sufficient urease loading, the face of the membrane opposite to the bulk solution could be maintained at a pH that would allow many enzymes to realize their maximum activities ( approximately 7.5). It was also found that this pH gradient could be maintained even in the presence of a buffer, which greatly enhances the transport of protons into the membrane. (c) 1993 John Wiley & Sons, Inc.     

Production of cephalosporin C by immobilized cells of Cephalosporium acremonium

Cephalosporium acremonium ATCC 48272 cells were immobilized on various adsorbents and in various entrapment matrices. The influence of the incubation period, the best immobilization technique and the optimum concentrations of the selected matrices were investigated. From the results of the repeated batch fermentation in shake flasks, a good level of antibiotic was maintained for a period of about 19 days using 4% calcium alginate and 1% glass wool as entrapment and adsorbent supports, respectively.     

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.     

Soft immobilized pH gradient gels in proteome analysis: a follow-up

As a follow-up of a previous work on two-dimensional map analysis utilizing soft (< 4%T) immobilized pH gradient (IPG) matrices in the first dimension (Candiano et al., Electrophoresis 2002, 23, 292-297), we have further optimized the preparation of such dilute IPG gels. One important step for obtaining an even reswelling of the entire IPG strip along the pH 3-10 interval is a washing step in 100 mM citric acid. It appears as though after rinsing off the excess acid in distilled water, a gradient of this tricarboxylic acid remains trapped into the IPG matrix, from almost nil at the acidic gel region to substantially higher amounts in its basic counterpart. This gradient helps in obtaining a uniform reswelling of the IPG strip, since carboxyl groups are more heavily hydrated than amino groups. The combined effects of uniform reswelling and of diluting the gel matrix favor penetration of large macromolecules (> 200 kDa) and allow for better spot resolution and for the display of a substantially higher number of spots also in the 30-60 000 Da region. A delipidation step in tri-n-butylphosphate:acetone:methanol (1:12:1) appears to substantially improve spot focusing and greatly diminish streaking and smearing of spots in all regions of the pH gradient.     

Protein desalting by isoelectric focusing in a segmented immobilized pH gradient

We have recently described an apparatus for protein purification based on a segmented Immobiline gel, having one or more liquid interlayers in between. The principle is entirely new, as it is based on keeping the protein of interest isoelectric, in a flow chamber, and focusing the impurities in an Immobiline gel. For this, a hydraulic flow is coupled orthogonally to an electric flow, sweeping away the non-isoelectric impurities from the recycling chamber. We now demonstrate that the present apparatus can be efficiently used for protein desalting. Hemoglobin A samples, containing 50 mM NaCl or 50 mM ammonium acetate, could be efficiently desalted in 2 h of recycling, after which the total salt content had decreased to less than 0.005 mM (a salt decrement of more than 10,000 fold the initial input). However, with polyprotic buffers (sulphate, citrate, phosphate, oligoamines) the desalting process was much slower, typically of the order of 20 h, possibly due to interaction of these species with the surrounding Immobiline matrix. In this last case, outside pH control (e.g. with a pH-stat) is necessary during protein purification, as, due to the faster removal of the monovalent counterion, the solution in the recycling chamber can become rather acidic or alkaline. It is demonstrated that the 2 extremities of the Immobiline segments facing the sample recycling chamber act indeed as isoelectric membranes, having a good buffering capacity, preventing the protein macroion from leaving the chamber by continuously titrating it to its isoelectric point.     

Two-dimensional maps in the most extended (pH 2.5-11) immobilized pH gradient interval

In conventional isoelectric focusing in soluble, amphoteric buffers, it has been quite difficult to produce two-dimensional (2-D) separations in pH intervals greater than pH 4-8. In general more alkaline proteins were analyzed by non-equilibrium IEF in the first dimension. Even with the advent of immobilized pH gradients (IPG), separations could be extended to pH gradients not wider than pH 3-10, due to a lack of suitable buffers. Since more acidic and more alkaline acrylamido buffers have recently been synthesized, we have been able to optimize what is believed to be the widest possible immobilized pH gradient, a pH 2.5-11 span. We report here for the first time 2-D separations of total tissue lysates in such extended pH 2.5-11 gradients. It appears that, with the IPG technique, close to 100% of all possible cell products can be displayed in a single 2-D map.     

A horizontal apparatus for isoelectric protein purification in a segmented immobilized pH gradient

A modification of the previously described apparatus (Faupel et al. (1987) J. Biochem. Biophys. Methods 15, 147-162), for recycling isoelectric focusing in a segmented immobilized pH gradient, is here reported. The most important improvements are: (1) a horizontal, vs. the previously vertical assembly; (2) a reduction of the thickness of the central flow chamber to 6 mm, vs. the previous 3 cm length and (3) the introduction, at both gel extremities of each Immobiline segment, of polypropylene filters, thus efficiently blocking the gel in situ. The advantages are: (i) the spontaneous removal of air bubbles, which in the vertical apparatus tend to accumulate in the ceiling of the flow chamber and to obstruct the flow of electric current; (ii) a more efficient hydraulic flow with a reduced chance of heating the liquid stream in the flow chamber, due to its reduced length along the separation path and (iii) a reduced risk of gel detachment from the tube walls, due to osmotic swelling caused by focused protein zones in the gel phase and by the fixed Immobiline charges in the polyacrylamide matrix.     

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.     

General theory of determining intraparticle active immobilized enzyme distribution and rate parameters

A general theory is presented in this article for determining the intrinsic rate constants for the main reaction and deactivation reaction, the effective diffusivity of the substrate, and the active enzyme distribution within porous solid supports from deactivation study of a continuous stirred-basket reactor (CSBR). For the parallel deactivation five reaction kinetics are considered: (a) Michaelis-Menten, (b) substrate inhibition, (c) product inhibition (competitive), (d) product inhibition (anticompetitive), and (e) zero-order kinetics. The experimental results of the system of hydrogen-peroxide-immobilized catalase on controlled-pore glass particles are analyzed to demonstrate the application of the theory developed for parallel deactivation of active immobilized enzyme (IME). For series deactivation only first-order kinetics is treated, and a numerical procedure is proposed to deter mine the rate parameters and the internal active enzyme distribution. The experimental data of the system of glucose-immobilized glucose oxidase on silica-alumina and controlled-pore glass particles are used to verify the theory.     

Direct measurement of intraparticle fluid velocity in superporous agarose beads

Superporous agarose beads contain both normal diffusion pores and special, very wide superpores through which part of the chromatographic flow is transported, a situation that may greatly improve the chromatographic performance. For the first time such pore flow was measured directly by following the movement of microparticles (dyed yeast cells) through superporous beads packed in a chromatographic bed. The passage of the microparticles through the superpores and through the interstitial pores was recorded by a microscope/video camera. The video recordings were subsequently used to determine flow paths as well as the convective fluid velocities in both the superpores and the interstitial pores. The superpore fluid velocity was found to be proportional to the ratio between the squares of the respective pore diameters, which is in agreement with the Kozeny-Carman equation. Values for two-dimensional and three-dimensional tortuosity of the flow paths were measured and calculated respectively.     

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.     

Role of transmembrane pH gradient and membrane binding in nisin pore formation.

Nisin is a cationic antimicrobial peptide that belongs to the group of lantibiotics. It is thought to form oligomeric pores in the target membrane by a mechanism that requires the transmembrane electrical potential delta psi and that involves local pertubation of the lipid bilayer structure. Here we show that nisin does not form exclusively voltage-dependent pores: even in the absence of a delta psi, nisin is able to dissipate the transmembrane pH gradient (delta pH) in sensitive Lactococcus lactis cells and proteoliposomes. The rate of dissipation increases with the magnitude of the delta pH. Nisin forms pores only when the delta pH is inside alkaline. The efficiency of delta psi-induced pore formation is strongly affected by the external pH, whereas delta pH-induced pore formation is rather insensitive to the external pH. Nisin(1-12), an amino-terminal fragment of nisin, and (des-deltaAla5)-(nisin(1-32) amide have a strongly reduced capacity to dissipate the delta psi and delta pH in cytochrome c oxidase proteoliposomes and L. lactis cells. Both variants bind with reduced efficiency to liposomes containing negatively charged phospholipids, suggesting that both ring A and rings C to E play a role in membrane binding. Nisin(1-12) competes with nisin for membrane binding and antagonizes pore formation. These findings are consistent with the wedge model of nisin-induced pore formation.     

Determination of intraparticle immobilized enzyme distribution in porous support by confocal scanning microscopy

Summary A method for determining the distribution of immobilized protein within a porous support has been developed. The method is based on confocal microscopy of polyacrylamide gel beads coupled to fluorescein isothiocyanate labelled enzyme. It is applied to immobilized soybean lipoxygenase. This technique allows the quantitative and qualitative analysis of protein distribution profile in intact polymer beads without splitting or cutting the carrier.     

Isoelectric protein purification by orthogonally coupled hydraulic and electric transports in a segmented immobilized pH gradient

A new method is described for preparative protein purification, based on isoelectric focusing on immobilized pH gradients. The principle is entirely new, as it is based on keeping the protein of interest isoelectric, in a flow-chamber, and focusing the impurities in the Immobiline gel. For this, a hydraulic flow is coupled orthogonally to an electric flow, sweeping away the non-isoelectric impurities from the recycling chamber. The sample flow-chamber is built in the centre of the apparatus, and is coupled to an upper and lower segment of an immobilized pH gradient. The protein to be purified is kept isoelectric in the flow-chamber and prevented from leaving it by arranging for the extremities of the immobilized pH gradient, forming the ceiling and the floor of this chamber, to have isoelectric points just higher (e.g. +0.05 pH units, on the cathodic side) and just lower (e.g. -0.05 pH units, on the anodic side) than the known pI of the species of interest. Macromolecules and small ions leave the flow chamber at a rate corresponding to a first order reaction kinetics (the plot of log C vs. time being linear). In general, for macromolecules, 12 h of recycling under current allow removal of 95% impurities. After 24 h of recycling, the protein of interest is more than 99.5% pure. The recoveries are very high (approaching 100%) as the sample under purification never enters the Immobiline gel and thus does not have to be extracted from a hydrophilic matrix, as typical of preparative gel electrophoresis.     

Influence of pH regulation and nutrient content on cephalosporin C production in solid-state fermentation by Acremonium chrysogenum C10

Aims: To investigate the effect of pH regulation and nutrient concentration on cephalosporin C (CPC) production in solid‐state fermentation (SSF), using sugarcane bagasse as inert support, impregnated with liquid medium. Methods and Results: Solid‐state fermentation using different initial pH values, buffer and nutrient concentrations were performed. Results revealed pH as a key parameter in CPC SSF, as it hampered the antibiotic production not only above 7·8, but also under 6·4. Using initial pH lower than 6·8 and PB in the solid medium, it was possible to keep pH within the production range, increase the production period (from 1 to 3 days) and hence the CPC yield from 468 to 3200 μg gdm^?1 (g^?1 of dry matter). Conclusion: Parameters that help to keep pH in adequate values for CPC production in SSF, such as initial pH, buffering system and nutrient concentration, can greatly increase the production time and CPC yields in this fermentation technique. Significance and Impact of the Study: This is the first work on CPC production on impregnated support, and the only one revealing pH as a key parameter; it is also shown that high nutrient concentration can improve CPC yields in SSF as long as pH is kept under control.     

Characterization of the rat liver membrane proteome using peptide immobilized pH gradient isoelectric focusing

Membrane proteins are of particular interest in proteomics because of their potential therapeutic utility. Past proteomic approaches used to investigate membrane proteins have only been partially successful at providing a comprehensive analysis due to the inherently hydrophobic nature and low abundance for some of these proteins. Recently, these difficulties have been improved by analyzing membrane protein enriched samples using shotgun proteomics. In addition, the recent application of methanol-assisted trypsin digestion of membrane proteins has been shown to be a method to improve membrane protein identifications. In this study, a comparison of different concentrations of methanol was assessed for assisting membrane protein digestion with trypsin prior to analysis using a gel-based shotgun proteomics approach called peptide immobilized pH gradient isoelectric focusing (IPG-IEF). We demonstrate the use of peptide IEF on pH 3-10 IPG strips as the first dimension of two-dimensional shotgun proteomics for protein identifications from the membrane fraction of rat liver. Tryptic digestion of proteins was carried out in varying concentrations of methanol in 10 mM ammonium bicarbonate: 0% (v/v), 40% (v/v), and 60% (v/v). A total of 800 proteins were identified from 60% (v/v) methanol, which increased the protein identifications by 17% and 14% compared to 0% (v/v) methanol and 40% (v/v) methanol assisted digestion, respectively. In total, 1549 nonredundant proteins were identified from all three concentrations of methanol including 690 (42%) integral membrane proteins of which 626 of these proteins contained at least one transmembrane domain. Peptide IPG-IEF separation of peptides was successful as the peptides were separated into discrete pI regions with high resolution. The results from this study prove utility of 60% (v/v) methanol assisted digestion in conjunction with peptide IPG-IEF as an optimal shotgun proteomics technique for the separation and identification of previously unreported membrane proteins.     

A comparison of immobilized pH gradient isoelectric focusing and strong-cation-exchange chromatography as a first dimension in shotgun proteomics

Recently, we have developed a high-resolution two-dimensional separation strategy for the analysis of complex peptide mixtures. This methodology employs isoelectric focusing of peptides on immobilized pH gradient (IPG) gels in the first dimension, followed by reversed-phase chromatography in the second dimension, and subsequent tandem mass spectrometry analysis. The traditional approach to this mixture problem employs strong-cation-exchange (SCX) chromatography in the first dimension. Here, we present a direct comparison of these two first-dimensional techniques using complex protein samples derived from the testis of Rattus norvegicus. It was found that the use of immobilized pH gradients (narrow range pH 3.5-4.5) for peptide separation in the first dimension yielded 13% more protein identifications than the optimized off-line SCX approach (employing the entire pI range of the sample). In addition, the IPG technique allows for a much more efficient use on mass spectrometer analysis time. Separation of a tryptic digest derived from a rat testis sample on a narrow range pH gradient (over the 3.5-4.5 pH range) yielded 7626 and 2750 peptides and proteins, respectively. Peptide and protein identification was performed with high confidence using SEQUEST in combination with a data filtering program employing pI and statistical based functions to remove false-positives from the data.