Purification of benzylpenicillin filtered broths by ultrafiltration and effect on solvent extraction

Purification of benzylpenicillin filtered broths obtained from fermented broths produced at CIPAN, SA Pilot Plant Fermentation was carried out by ultrafiltration with diafiltration. This study was done using an ultrafiltration laboratory/pilot installation from Paterson Candy International Ltd. whose module has a tubular configuration. Membranes with molecular weight cut-offs of 8000 (polysulfone), 20?000 (polysulfone) and 100?000 (PVDF) were assessed. Comparison between solvent extraction of benzylpenicillin from ultrafiltered broths and from filtered broths using flocculants was also done. Ultrafiltration with diafiltration of benzylpenicillin filtered broths was used successfully to remove proteins, colored substances and other impurities giving high benzylpenicillin recovery in the permeate, as an alternative to the use of flocculants and anti-emulsion agents to obtain good phases separation in benzylpenicillin solvent extraction.     

Concentration of ultrafiltered benzylpenicillin broths by reverse osmosis

Concentration of benzylpenicillin filtered broths purified by ultrafiltration and fermented broths clarified by ultrafiltration was carried out by reverse osmosis. This study was done using a reverse osmosis laboratory/pilot installation from Paterson Candy International Ltd. whose module has a tubular configuration and a membrane with a molecular weight cut-off of 100 Dalton (ZF99) made of a polyamide film with a rejection of 99% of NaCl. It was concluded that reverse osmosis is an adequate technique to concentrate benzylpenicillin ultrafiltered broths, leading to low losses of benzylpenicillin in the permeate and high benzylpenicillin recovery for high volumetric concentration factors.     

Enzymatic conversion of benzylpenicillin to 6-aminopenicillanic acid in concentrated ultrafiltered broths

Benzylpenicillin filtered broths purified by ultrafiltration and fermented broths clarified by ultrafiltration and afterwards concentrated by reverse osmosis were used directly for enzymatic conversion of benzylpenicillin to 6-aminopenicillanic acid and phenylacetic acid by immobilised penicillin G acylase or amidase. It was concluded that, when the ultrafiltration operation retained 100% of protein, the concentrates from reverse osmosis could be successfully directly fed to the enzymatic reactor, giving high enzymatic conversion yield of benzylpenicillin to 6-aminopenicillanic acid.     

Application of a 22L scale membrane bioreactor and cross-flow ultrafiltration to obtain purified chondroitin

Recently, the possibility of producing fructosylated chondroitin from the capsular polysaccharide of Escherichia coli O5:K4:H4, in fed‐batch and microfiltration experiments was assessed on a 2 L bioreactor. In this work, a first scale‐up step was set on a 22 L membrane reactor with modified baffles to insert ad hoc designed microfiltration modules permanently inside the bioreactor vessel. Moreover, the downstream polysaccharide purification process, recently established on the A¨?KTA cross‐flow instrument, was translated to a UNIFLUX‐10, a tangential flow filtration system suitable for prepilot scale. In particular, the microfiltered permeates obtained throughout the fermentation, and the supernatant recovered from the centrifuged broth at the end of the process, were treated as two separate samples in the following ultrafiltration procedure, and the differences in the two streams and how these affected the ultrafiltration/diafiltration process performance were analysed. The total amount of K4 capsular polysaccharide was about 85% in the broth and 15% in the microfiltered permeates. However, the downstream treatment was more efficient when applied to the latter. The major contaminant, the lipopolysaccharide, could easily be separated by a mild hydrolysis that also results in the elimination of the unwanted fructosyl residue, which is linked to the C‐3 of glucuronic acid residues. The tangential ultrafiltration/diafiltration protocols developed in a previous work were effectively scaled‐up, and therefore in this research proof of principle was established for the biotechnological production of chondroitin from the wild‐type strain E. coli O5:K4:H4. The complete downstream procedure yielded about 80% chondroitin with 90% purity. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 28: 1012–1018, 2012     

The purification of recombinant hepatitis B surface antigen by hollow fibre ultrafiltration membrane diafiltration

Summary Recombinant hepatitis B surface antigen (HBsAg) broth was purified by diafiltration with a hollow fibre ultrafiltration membrane (cut off 100 kDa), by pre—treating the HBsAg broth with enzyme, most of the contaminating proteins was removed and very high recovery ratio of HBsAg was achieved. When HBsAg solution was concentrated using hollow fibre ultrafiltration membrane to 10% of its original volume, the HBsAg was recovered almost completely. Accordingly, membrane purification of HBsAg is a high yield, fast method.     

Molecular composition of diphtheria toxoid produced using semi-synthetic and meat extract-based broths

The use of semi-synthetic broths for cultivation of Corynebacterium diphtheriae instead of a meat extract-based broth avoids the presence of highly undesirable bovine meat antigens in the diphtheria toxoid. As information on the composition of casein digest-based broths used for the production of diphtheria toxoid is scarce, we have now developed one. The composition of a casein-based medium that supports vigorous bacterial growth as well as high toxin production is described below. The comparative analysis of the toxoids, produced using the meat-based Pope–Lingood and the casein digest-based broths, showed considerable differences in their molecular composition. The variance of weight distribution of toxoid-containing molecular complexes was smaller when the semi-synthetic broth was used. Normal human therapeutic IgG recognizes some of the proteins in the meat-based medium but does not react with any components of the semi-synthetic medium. While precipitation at the isoelectric point of the diphtheria toxoid produced by culturing the C. diphtheriae strain in the semi-synthetic medium resulted in a preparation meeting the requirement for purity (more than 1500 limit floculation Lf/mg protein nitrogen PN), the toxoid produced in the Pope–Lingood broth failed to meet this requirement in some cases, even after a second purification step using ultrafiltration.     

Large-scale purification and characterization of recombinant tick anticoagulant peptide

Recombinant tick anticoagulant peptide (r-TAP), a potent and specific inhibitor of blood coagulation factor Xa, was purified to > 99% homogeneity at the multi-gram scale. Genetically engineered yeast secreted 200–250 mg/l of the heterologous protein into the medium. Cells were separated from broth by diafiltration and purification was done by two chromatographic steps, both conducive to operation on a large scale. Analysis of the purified protein by several methods indicated that it was > 99% homogeneous and no incompletely processed or truncated proteins were detected. Physico-chemical characterization data of r-TAP show that it exists as a monomer in solution and no evidence of post-translational modification was observed. The purified protein was fully active in inhibiting human coagulation factor Xa.     

Assessment of the Accuprobe Listeria monocytogenes culture identification reagent kit for rapid colony confirmation and its application in various enrichment broths.

The Accuprobe Listeria monocytogenes Culture Identification Reagent Kit, a nonradioactive probe, was evaluated as a colony confirmation test and in different selective or nonselective enrichment broths. The probe was 100% sensitive and 100% specific when applied to isolated colonies. The minimal detection limit in physiological saline was established to be about 10(5) CFU of L. monocytogenes. Hybridization done directly in broths seeded with L. monocytogenes showed variable results. Three nonselective broths (Todd-Hewitt broth, brain heart infusion broth, and tryptic soy broth) and one selective broth (FDA) gave positive reactions at an inoculum of 5 x 10(6) CFU, whereas two other selective broths (UVM, and PALCAMY) gave negative reactions with up to 10(8) and 10(9) CFU. In FDA broth, the level of detection of L. monocytogenes was not modified by the presence of other organisms in mixed cultures.     

Assessment of the Accuprobe Listeria monocytogenes culture identification reagent kit for rapid colony confirmation and its application in various enrichment broths.

The Accuprobe Listeria monocytogenes Culture Identification Reagent Kit, a nonradioactive probe, was evaluated as a colony confirmation test and in different selective or nonselective enrichment broths. The probe was 100% sensitive and 100% specific when applied to isolated colonies. The minimal detection limit in physiological saline was established to be about 10(5) CFU of L. monocytogenes. Hybridization done directly in broths seeded with L. monocytogenes showed variable results. Three nonselective broths (Todd-Hewitt broth, brain heart infusion broth, and tryptic soy broth) and one selective broth (FDA) gave positive reactions at an inoculum of 5 x 10(6) CFU, whereas two other selective broths (UVM, and PALCAMY) gave negative reactions with up to 10(8) and 10(9) CFU. In FDA broth, the level of detection of L. monocytogenes was not modified by the presence of other organisms in mixed cultures.     

A simple model for the optimization of the extraction yield of antibiotics isolated from fermented broths by direct crystallization

This article is concerned with the development of a model to maximize the overall yield of isolation of antibiotics recovered from fermented broths by the so-called direct precipitation method. In this process, as in most antibiotics isolation processes, a second filtration of the semiexhaust mycellium from the first filtration, after slurrying it in water at the suitable pH, is required. The maximization of the overall yield of isolation implies the use of an optimal amount of water, measured as a volume to fermented broth mass ratio, which can be calculated by using the model derived here. The model also allows for the calculation of the partial and overall yields of the isolation process, and its validity is demonstrated by its ability to describe reasonably well the isolation data of two different tetracycline-fermented broths produced according to two different technologies.The application of the model requires only the knowledge of easily obtainable fermented broth parameters and is illustrated for two different types of tetracycline-fermented broths. Although the model had been derived for the optimization of the overall yield of isolation of antibiotics recovered by direct precipitation, it can easily be adapted to be used for the optimization of the overall yield of isolation of antibiotics recovered by other isolation processes. (c) 1993 John Wiley & Sons, Inc.     

Production of propionic acid from whey permeate by sequential fermentation, ultrafiltration, and cell recycling

This article deals with the production by fermentation of a mycostatic and aromatic food additive based on propionic acid. Membrane bioreactors have been used from laboratory scale up to pilot and industrial production plants. Due to the high cell densities achieved by the sequential recycling mode of operation, a mixed acids solution was rapidly produced from whey permeate. The sterile fermented broth obtained was subsequently concentrated at different levels by evaporation and spray drying according to the projected use. Concentrated Propionibacterium cells (200 g . L(-1) DW) were obtained from the process by periodic bleeds and could be used to good effect as cheese starters, silage preservatives, or probiotics. Propionic acid concentrations from 30 to 40 g . L(-1) were easily achieved with no residual lactose. The highest volumetric productivity was 1.6 g . L(-1) . h(-1) for total acid and 1.2 g . L(-1) . h(-1) for propionic acid with a specific productivity of 0.035 h(-1). (c) 1993 John Wiley & Sons, Inc.     

Isolation and purification of a new protease from Aspergillus niger LCF no 9

Summary Aspergillus niger LCF N ^o 9 synthesizes large amounts of a semi-alkaline protease highly active on Benzoyl arginine p-nitroanilide (BAPNA) that is likely to find industrial use. An industrial-grade enzyme of around 80% purity was prepared and a reference enzyme was obtained in high yield from the industrial product by ultrafiltration and HPIEC on a mono Q column. The industrial-grade enzyme was produced on a pilot scale with a yield of 0.52% of medium solid starting material by adsorption on CM-Sephadex A₅₀, precipitation with acetone at –30°C, ion-exchange chromatography on DEAE-Sepharose and diafiltration.     

Optimization of spray drying process for Bacillus thuringiensis fermented wastewater and wastewater sludge

Response surface methodology was used to optimize spray drying process for producing biopesticide powders of Bacillus thuringiensis by using fermented broth of starch industry wastewater and wastewater sludge. Analysis of variance was carried out using number of viable spores in the powder as dependent variable. The determination coefficients of models were 92 and 94% for fermented broth of starch industry wastewater and wastewater sludge, respectively. Under the optimal conditions of the operational parameters of spray drying, the numbers of viable spores were 2.2 × 10⁸ and 1.3 × 10⁸ CFU/mg in the dry powders for starch industry wastewater and wastewater sludge respectively, with a loss of viable spores of 18 and 13% when compared with their respective fermented broths. The entomotoxicity (measured by the bioassay method) of the powders obtained under optimal conditions showed a loss of 28 and 18% when compared with the fermented broth of starch industry wastewater and wastewater sludge, respectively. The optimized results of spray drying were used for field application calculations. The volume of fermented broth required to produce powder formulated product when compared with the volume required for liquid formulation product in order to treat 1 ha of balsam fir was less and offered several advantages.     

Comparative evaluation of stability of benzylpenicillin in acid media of natural solutions and in culture fluid]

Inactivation of benzylpenicillin in real media i.e. fermentation broths and their filtrates was studied in comparison with the published data on inactivation of commercial benzylpenicillin in aqueous solutions as dependent on the medium pH and temperature. The lowest constant of benzylpenicillin inactivation was shown to be in the fermentation broths.     

Thin layer chromatographic determination of organic acids for rapid identification of bifidobacteria at genus level

This study presents a simple and fast method for the identification of bifidobacteria using a thin layer chromatographic (TLC) analysis of the short chain fatty acids in a culture broth. When the chromatogram was sprayed with the indicator solution (methyl red-bromophenol blue in 70% ethanol), lactic acid exhibited two red spots, and acetic acid, propionic acid, and butyric acid all produced blue spots. Succinic acid and citric acid produced yellow and dark yellow spot, respectively. In addition, these organic acids showed different R(f) values. The total time taken to analyze the organic acids in the 10 bacterial culture broths using the proposed method was approximately 50 min. The proposed TLC method was used to analyze the organic acids in culture broths of the following strains, five Bifidobacterium species. (Bifidobacterium longum, B. breve, B. infantis, B. bifidum, and B. adolescentis) and five other lactic acid bacteria strains (Lactobacillus casei, L. bulgaricus, L. acidophilus, Streptococcus thermophilus, and S. lactis). Both spots of lactic acid and acetic acid were detected on all the TLC plates from the five bifidobacterial culture broths. The five other lactic acid bacterial culture broths, however, only exhibited lactic acid spots. Accordingly, the proposed TLC method would appear to be a useful tool for rapid identification of Bifidobacterium spp. at the genus level.     

Ultrafiltration characteristics of immunobiological preparations

The removal of ammonium sulfate from the bulk product of fermented antitoxic serum by continuous diafiltration was not accompanied by changes in the stability of the solution. To concentrate immunoglobulin, eluted from DEAE cellulose, by diafiltration, the stabilization of the solution by adding sodium chloride at high concentration was necessary. The use of membranes purchased from different manufacturers and having similar selectivity characteristics permitted obtaining transfer factor preparations somewhat differing in their biological activity. The process of ultrafiltration, carried out in the atmosphere of compressed carbon dioxide, made it possible to obtain such preparations from donor blood plasma.     

Separation of clavulanic acid from fermented broth of amino acids by an aqueous two-phase system and ion-exchange adsorption

The clavulanic acid is a substance which inhibits the β-lactamases used with penicillins for therapeutic treatment. After the fermentation, by-products of low molecular weight such as amino acids lysine, histidine, proline and tyrosine are present in the fermented broth. To remove these impurities the techniques of extraction by an aqueous two-phase system of 17% polyethylene glycol molecular weight 600 and 15% potassium phosphate were used for a partial purification. A subsequent ion-exchange adsorption was used for the recuperation of the clavulanic acid of the top phase and purification getting a concentration factor of 2 and purification of 100% in relation to the amino acids lysine, histidine, proline and tyrosine.     

Ultrafiltration recovery of entomotoxicity from supernatant of Bacillus thuringiensis fermented wastewater and wastewater sludge

The study investigates the recovery of active components (crystal proteins, spores and other factors of virulence) of Bacillus thuringiensis (Bt) based biopesticides from centrifuged supernatant, by ultrafiltration. The centrifuged fermented broths comprised, starch industry wastewater, non-hydrolyzed and hydrolyzed wastewater sludge and semi-synthetic soya medium (as control). The ultrafiltration membrane of 5 kDa gave highest recovery of the active components and increased the entomotoxicity in the retentates by 7.9%, 10.5%, 9.0%, 5.7%, for semi-synthetic soya medium, starch industry wastewater, non-hydrolyzed and hydrolyzed wastewater sludge, respectively. However, the retention of suspended solids on the membrane (measured via mass balance) varied with the type of fermented broths and was very high for hydrolyzed sludge (soya-15%; starch industry wastewater-12%; non-hydrolyzed sludge-7% and hydrolyzed sludge-68%). This reflected the deposit on the membrane. In the given context, scale-up of the ultrafiltration process will give better efficacy for non-hydrolyzed sludge and starch industry wastewater in comparison to soya and hydrolyzed sludge medium.     

Dean vortex membrane microfiltration and diafiltration of rBDNF E. coli inclusion bodies

Cross-flow microfiltration (CMF) and diafiltration were used to concentrate and purify recombinant Brain-Derived Neutrophic Factor (rBDNF) inclusion bodies from an E. coli cell suspension and a homogenized E. coli cell suspension (homogenate/lysate). Although these processes have been tested industrially in pilot scale with conventional linear membrane microfiltration modules, their performances were severely limited due to membrane fouling. The purpose of this work was to determine whether Dean vortex microfiltration with controlled centrifugal instabilities (Dean vortices produced in helical flow) could be used to improve filtration performance over that observed with conventional linear cross-flow microfiltration (CMF). For the microfiltration experiments with the feeds containing cell and homogenate suspensions, improvements in flux of about 50 and 70%, respectively, were obtained with the helical module as compared with that obtained with the linear module. For diafiltration with the homogenate suspension as feed, solute transport (as measured by mass) was from 100 to 40% higher after 40 and 100 min, respectively, with the helical module as compared with that obtained with the linear module. In the presence of the neutral surfactant, Tween 20, solute transport for diafiltration was at least 25 times higher during the first 10 min of operation and 100% higher after 300 min with the helical module as compared with that obtained with the linear module. Clearly, improved filtration performance, a purer and more concentrated product, and substantial savings can be expected with the new Dean vortex filters.     

Filtration of a bacterial fermentation broth: harvest conditions effects on cake hydraulic resistance

The hydraulic resistance of cakes formed during the ultrafiltration of Streptomyces pristinaespiralis broths has been investigated for different harvesting conditions. S. pristinaespiralis broth was harvested after the point of microorganism activity declines (0-h aged broth) and afterwards held for different durations of up to 16 h (16 aged broths). Aging behavior occurring between the end of microorganism activity and harvest was compared for different acidification procedures (pH) and the mechanisms for which the hydraulic resistance of the cake is affected by aging have been investigated. For broths harvested under conditions where the acidification is fixed at pH 2 or 3, hydraulic resistance associated with cake build-up is directly determined by the interactions between the cells. Holding broths beyond 5 h contributes to a release of a soluble component from the cell surface. Enhanced cell surface interactions then turn the cake structure into a more open one and reduce the specific hydraulic resistance. For broths harvested under conditions where the acidification is fixed at pH 4, hydraulic resistance associated with cake build-up is both determined by cell interactions and cell morphology. The cause of the increase in specific hydraulic resistance with aging is due to the binding of a soluble component released by the microorganisms, which decreases the cell surface interactions.