Resolution and productivity of conalbumin and lysozyme from fresh egg-white loaded at very high flow rate on a 250-mm length CM-HVFM column.

A 250 x 10 mm I.D. column of CM-HVFM, a novel carboxymethyl ion-exchange matrix, has been used as a preparative chromatographic column to separate fresh egg-white protein. When loading a diluted egg-white solution at pH 4.8 ovalbumin was not adsorbed and lysozyme was preferentially adsorbed compared to the conalbumin. As the column loading was increased from 24 to 450 kg m-3 column volume at the superficial velocity of 6.12 m h-1, the lysozyme continued to be absorbed eventually displacing conalbumin. A maximum lysozyme productivity at 16.7 kg m-3 h-1 was achieved at the highest loading. For conalbumin a maximum productivity of 8.8 kg m-3 h-1 occurred at the lower loading of 100 kg m-3. The purities of lysozyme and conalbumin were comparable at a column loading of 450 kg m-3 h-1. The performance of the column was not degraded, neither was the column blocked or channelled despite the high column loading at the high flow-rate.     

Application of a novel PRODUCTIVTM CM column in egg-white protein separation: Effect of high flow-rate on resolution and productivity

Summary A preparative PRODUCTIV^TM CM, a new coherent ion-exchanger, column (250×10 mm ID) has been used to separate egg-white proteins without cell debris remover (CDR) pretreatment. Results showed that the productivity increased with the superficial velocity (V_s) and a very high V_s (9.2 m/h) can benefit the high productivity (87.4 g/l.h) in comparison with 6.4 and 33 g/l.h as reported by others. Despite the high flow-rate and high column loading, the resolution of the eluted peaks of lysozyme and conalbumin, was maintained at 1.16.     

Process evaluations and economic analyses of recombinant human lysozyme and hen egg-white lysozyme purifications

Human lysozyme and hen egg-white lysozyme have antibacterial, antiviral, and antifungal properties with numerous potential commercial applications. Currently, hen egg-white lysozyme dominates low cost applications but the recent high-level expression of human lysozyme in rice could provide an economical source of lysozyme. This work compares human lysozyme and hen egg-white lysozyme adsorption to the cation exchange resin, SP-Sepharose FF, and the effect of rice extract components on lysozyme purification. With one exception, the dynamic binding capacities of human lysozyme were lower than those of hen egg-white at pH 4.5, 6, and 7.5 with ionic strengths ranging from 0 to 100 mM (5-20 mS). Ionic strength and pH had a similar effect on the adsorption capacities, but human lysozyme was more sensitive to these two factors than hen egg-white lysozyme. In the presence of rice extract, the dynamic binding capacities of human and hen egg-white lysozymes were reduced by 20-30% and by 32-39% at pH 6. Hen egg-white lysozyme was used as a benchmark to compare the effectiveness of human lysozyme purification from transgenic rice extract. Process simulation and cost analyses for human lysozyme purification from rice and hen egg-white lysozyme purification from egg-white resulted in similar unit production costs at 1 ton per year scale.     

Monosize poly(glycidyl methacrylate) beads for dye-affinity purification of lysozyme

Cibacron Blue F3GA was covalently attached onto monosize poly(glycidyl methacrylate) [poly(GMA)] beads for purification of lysozyme from chicken egg white. Monosize poly(GMA) beads, 1.6 microm in diameter, were produced by a dispersion polymerization technique. The content of epoxy groups on the surface of the poly(GMA) sample determined by the HCl-pyridine method (3.8 mmol/g). Cibacron Blue F3GA loading was 1.73 mmol/g. The monosize beads were characterized by elemental analysis, FTIR and SEM. Adsorption studies were performed under different conditions in a batch system (i.e., medium pH, protein concentration, temperature and ionic strength). Maximum lysozyme adsorption amount of poly(GMA) and poly(GMA)-Cibacron Blue F3GA beads were 1.6 and 591.7 mg/g, respectively. The applicability of two kinetic models including pseudo-first order and pseudo-second order model was estimated on the basis of comparative analysis of the corresponding rate parameters, equilibrium adsorption capacity and correlation coefficients. Results suggest that chemisorption processes could be the rate-limiting step in the adsorption process. It was observed that after 10 adsorption-elution cycle, poly(GMA)-Cibacron Blue F3GA beads can be used without significant loss in lysozyme adsorption capacity. Purification of lysozyme from egg-white was also investigated. Purification of lysozyme was monitored by determining the lysozyme activity using Micrococcus lysodeikticus as substrate. The purity of the eluted lysozyme was analyzed by SDS-PAGE and found to be 88% with recovery about 79%. The specific activity of the eluted lysozyme was high as 43,600 U/mg.     

Chromatography of hen egg-white proteins on anion-exchange cellulose at high flow rates using a radial flow column.

The influence of column configuration on the separation of hen egg-white proteins using Whatman DE52 and QA52 anion-exchange cellulose has been investigated. Using a 100 ml volume axial flow column (6.6 cm x 4.4 cm i.d.) we achieved flow rates of up to 25 ml/min i.e. 15 bed volumes/h after which higher flow was restricted due to pressure constraints within the system. Under radial flow conditions using a 100 ml column flow rates of up to 150 ml/min i.e. 90 bed volumes/h were achieved using DE52 and QA52. While chromatographic resolution was superior under axial flow at the lower flow rates excellent resolution was maintained at up to 150 ml/min using the radial flow column. This is a consequence of the fast kinetics of adsorption/desorption exhibited by DE52 and QA52. The data indicate that it is the column configuration and not the cellulose matrix which influences flow performance.     

Affinity adsorption of lysozyme on a macroligand prepared with Cibacron Blue 3GA attached to yeast cells

The objective of this study was the development of affinity adsorbent particles with the appropriate characteristics to be applied in protein purification using the affinity ultrafiltration method. To prepare affinity macroligands Cibacron Blue 3GA, as a ligand molecule, was immobilized by covalent bonding onto yeast cell walls, the support material or matrix. The maximum attachment of the ligand to the matrix was 212 μmol/g (ligand dry weight/yeast dry weight). Lysozyme was selected as the protein model for the adsorption studies. Its adsorption onto the matrix without ligand and matrix with attached ligand were investigated batch-wise. The adsorption equilibrium isotherms appeared to follow a typical Langmuir isotherm. The maximum adsorption capacity (q(m)) of the Cell-Cibacron macroligand for lysozyme was 110 mg/ml of wet macroligand. The adsorbent was also employed for the separation of lysozyme from hen egg white. High purity lysozyme was obtained.     

A simple, one-step chromatographic procedure for the purification of lysozyme

A rapid method for the purification of lysozyme (mucopeptide N-acetyl-muramoylhydrolase, EC 3.2.1.17) from hen egg-white has been devised. It was that gel filtration chromatography on agarose columns can be used selectively to purify lysozyme, due to the fact that this protein interacts with the agarose matrix and elutes later than the corresponding total volume for the column. Thus, lysozyme is directly obtained in a relatively pure form and with a high specific activity. In principle, this simple method can be used to prepare lysozymes from other sources.     

Adsorption chromatography of proteins

A method for adsorption chromatography of proteins is proposed. A protein solution is passed through a cellulose column at a pH value corresponding to an isoelectric point of the protein. Depending on the charge of unwanted proteins, they either remain at the origin (if charges of protein and ion-exchanger are opposite) or are released from the column (if charges of protein and ion-exchanger coincide). Elution volume of the purified protein is higher than for the second group of unwanted proteins because movement of the uncharged protein of interest includes its adsorption on cellulose followed by subsequent desorption caused by the elution buffer. Problems of optimization of buffers and adsorbents are discussed. Applicability of the method of adsorption chromatography is illustrated using purification of horseradish peroxidase as an example.     

Protein refolding at high concentration using size-exclusion chromatography

A new method to improve refolding yields and to increase the concentration of refolded proteins in a single operation has been developed. The method uses size-exclusion chromatography matrices to perform buffer exchange, aggregate removal, and the folding reaction. The reduced diffusion of proteins in gel-filtration media has been shown to suppress the nonspecific interactions of partially folded molecules, thus reducing aggregation. Hen egg white lysozyme (HEWL) and bovine carbonic anhydrase (CAB) were successfully refolded from initial protein concentrations of up to 80 mg/mL using Sephacryl S-100 (HR). The aggregation reaction for lysozyme was reduced and was only detected at the highest protein concentration used. The average recovery of lysozyme was 63%, with an average specific activity of 104%. Carbonic anhydrase experiments also showed that aggregation was suppressed and the average protein recovery from the column was 56%, with a specific activity of 81%. This process enables refolding and the purification of active species to be achieved in a single step. (c) 1996 John Wiley & Sons, Inc.     

Purification of a retinol binding protein from the hen-oviduct cytosol and its immunological cross-reactivity with those from the nucleus

Cellular retinol-binding protein was purified from the cytosol of the oviducts of laying hens by ammonium sulphate fractionation and chromatography on Sephadex G-75 and DEAE-Sephadex A-50 columns. Analysis of the purified retinol-binding protein on 10% SDS-polyacrylamide gel revealed the presence of a doublet representing very similar molecular sizes. Antiserum was prepared against the purified cellular retinol-binding protein, and on the basis of (a) immunodiffusion test and (b) immunoneutralization of 3H-labelled retinol-cellular retinol-binding protein complex on a column of Sephadex G-75, the antiserum appeared to be specific. The antiserum showed cross-reactivity with the nucleosol and a 0.4 M NaCl extract of the chromatin of the oviduct nuclei, while it did not react with the major egg-white proteins such as ovalbumin, conalbumin and ovomucoid.     

Preparation of a light-sensitive and reversible dissolution copolymer and its application in lysozyme purification

A novel light-sensitive and cation-exchange copolymer (PNBCC) has been synthesized by random copolymerization of chlorophyllin sodium copper salt, crylic acid, n-butyl acrylate, and N-isopropylacrylamide. The PNBCC copolymer showed reversible dissolution and could be precipitated by 488 nm laser irradiation with the least light density of 1.70 x 10(5) W/m(2). By optimizing the ratio of monomers, pH, and ion concentration, over 95% copolymer was recovered by laser irradiation. The copolymer was used to purify lysozyme as light-sensitive cation exchanger, and its adsorption matched a Langmuir adsorption isotherm with maximum adsorption capacity of 98,900 U/g and dissociated constant of 852 U/mL. By applying the copolymer to the separation of lysozyme from egg white, the specific activity of lysozyme was improved from 399 to 6346 U/mg and the recovery of lysozyme achieved 81.3%.     

On protein solubility in organic solvent

Solubility of a model protein, hen egg-white lysozyme, was investigated in a wide range of neat nonaqueous solvents and binary mixtures thereof. All solvents that are protic, very hydrophilic, and polar readily dissolve more than 10 mg/mL of lysozyme (lyophilized from aqueous solution of pH 6.0). Only a marginal correlation was found between the lysozyme solubility in a non-aqueous solvent and the letter's dielectric constant or Hildebrand solubility parameter, and no correlation was observed with the dipole moment. Lysozyme dissolved in dimethyl sulfoxide (DMSO) could be precipitated by adding protein nondissolving co-solvents, although the enzyme had a tendency to form supersaturated solutions in such mixtures. The solubility of lysozyme, both in an individual solvent (1,5-pentanediol) and in binary solvent mixtures (DMSO/acetonitrile), markedly increased when the pH of the enzyme aqueous solution prior to lyophilization was moved away from the proteins's isoelectric point. (c) 1994 John Wiley & Sons, Inc.     

Macroporous chitin affinity membranes for lysozyme separation

Macroporous chitin membranes with high, controlled porosity and good mechanical properties have been prepared using a technique developed in this laboratory based on silica particles as porogen. They were employed for the affinity separation of lysozyme. Chitin membranes (1 mm thickness) can be operated at high fluxes (>/=1.1 mL/min/cm(2)) corresponding to pressure drops >/=2 psi. Their adsorption capacity for lysozyme ( approximately 50 mg/mL membrane) is by an order of magnitude higher than that of the chitin beads employed in column separation. In a binary mixture of lysozyme and ovalbumin, the membranes showed very high selectivity towards lysozyme. The effect of some important operation parameters, such as the flow rates during loading and elution were investigated. Lysozyme of very high purity (>98%) was obtained from a mixture of lysozyme and ovalbumin, and from egg white. The results indicate that the macroporous chitin membranes can be used for the separation, purification, and recovery of lysozyme at large scale. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 610-617, 1997.     

Partition of protein from binary mixtures by a batch foaming process

An experimental study to assess the partition of 3 binary protein mixtures when foam separated is presented (proteins considered were bovine serum albumin (BSA), conalbumin and lysozyme). Results show that selective partition of protein can be achieved and under certain conditions it is possible to strip the initial solution of BSA. However, purity of the foam phase is limited due to the non-selective carry-up of other proteins in the interstitial liquid.     

Conversion of Trp 62 of hen egg-white lysozyme to Tyr by site-directed mutagenesis

An expression plasmid for hen egg-white lysozyme in Saccharomyces cerevisiae was constructed by inserting almost full-length cDNA (about 600 base pairs) encoding hen egg-white pre-lysozyme into a yeast expression vector, pAM 82. The hen lysozyme was expressed under the control of the repressible acid phosphatase promoter of pAM 82 in S. cerevisiae. About half of the expressed lysozyme was secreted in the yeast growth medium as a precise mature protein which exhibited specific activity consistent with that of authentic hen egg-white lysozyme. The replacement of Trp 62 of hen egg-white lysozyme with a tyrosine residue was performed by site-directed mutagenesis using a 19-mer oligodeoxyribonucleotide. The mutant lysozyme with Tyr 62 was found to exhibit enhanced bacteriolytic activity.     

Particle-by-particle quantification of protein adsorption onto poly(ethylene glycol) grafted surfaces

The use and advantage of flow cytometry as a particle-by-particle, low sampling volume, high-throughput screening technique for quantitatively examining the non-specific adsorption of proteins onto surfaces is presented. The adsorption of three proteins: bovine serum albumin (BSA), immunoglobulin gamma (IgG) and protein G, incubated at room temperature for 2 h onto organosilica particles modified with poly(ethylene glycol) (PEG) of increasing MW (2000, 3400, 6000, 10,000 and 20,000 g mol(-1)) and grafted amounts (0.14-1.4 mg m(-2)) was investigated as a model system. Each protein exhibited Langmuir-like, high affinity monolayer limited adsorption on unmodified particles with the proteins reaching surface saturation at 1.8, 4.0 and 2.5 mg m(-2) for BSA, IgG and protein G, respectively. Protein adsorption on PEG-modified surfaces was found to decrease with increasing amounts of grafted polymer. PEG grafting amounts >0.6 mg m(-2) effectively prevented the adsorption of the larger two proteins (BSA and IgG) while a PEG grafting amount >1.3 mg m(-2) was required to prevent the adsorption of the smaller protein G.     

Evaluation of alternatives for human lysozyme purification from transgenic rice: impact of phytic acid and buffer

Producing economically competitive recombinant human lysozyme from transgenic rice demands an inexpensive purification process for nonpharmaceutical applications. Human lysozyme is a basic protein, and thus, cation exchange chromatography was the selected method for lysozyme purification. Similar to other protein production systems, the identification of critical impurities in the rice extract was important for the development of an efficient purification process. Previous adsorption data indicated that phytic acid was probably responsible for an unacceptably low cation exchange adsorption capacity. In this study, we confirm that reducing phytic acid concentration improves lysozyme binding capacity and investigate alternative process conditions that reduce phytic acid interference. Compared with the previous best process, the adsorption capacity of human lysozyme was increased from 8.6 to 19.7 mg/mL when rice extract was treated with phytase to degrade phytic acid. Using tris buffer to adjust pH 4.5 extract to pH 6 before adsorption reduced phytic acid interference by minimizing phytic acid-lysozyme interactions, eliminated the need for phytase treatment, and increased the binding capacity to 25 mg/mL. Another method of reducing phytic acid concentration was to extract human lysozyme from rice flour at pH 10 with 50 mM NaCl in 50 mM sodium carbonate buffer. A similar binding capacity (25.5 mg/mL) was achieved from pH 10 extract that was clarified by acidic precipitation and adjusted to pH 6 for adsorption. Lysozyme purities ranged from 95 to 98% for all three processing methods. The tris-mediated purification was the most efficient of the alternatives considered.     

Vapor-phase hydrazinolysis for microdetermination of carboxyl-terminal amino acids of proteins

The "vapor-phase" hydrazinolysis method was devised for the microdetermination of the carboxyl-terminal residue of a protein. With this method, a polypeptide sample is degraded with vaporized hydrazine. The optimum conditions for hen egg-white lysozyme were established to be 2 to 4 h at 90 or 100 degrees C, the recovery of the carboxyl-terminal leucine being about 70%. With this vapor-phase method, side reactions are reduced and the time of hydrazinolysis is shortened. The limit of quantitation for the carboxyl-terminus of a protein is about 50 pmol, as judged so far with hen egg-white lysozyme. The carboxyl-termini of several proteins were determined using this novel procedure.     

Induction of chromosome aberrations, micronucleus formation and sperm abnormalities in mouse following carbofuran exposure

Carbofuran was tested to study in vivo cytogenetic effects in mouse bone marrow cells and morphological alterations in sperms. The acute oral and intraperitoneal (i.p.) LD(50) of carbofuran was determined to be 9.5 or 2.0 mg/kg b.w. in mice, respectively. The animals were orally administered 1.9, 3.8 or 5.7 mg/kg b.w. (20, 40 and 60% of LD(50)) of carbofuran for 24 h or 1.9 mg/kg b.w. for 4 consecutive days (cumulative 7.6 mg/kg or 80% of LD(50)) to analyse chromosome aberrations (CAs). For micronucleus test (MT) animals were orally exposed to 5.7 mg/kg b.w. for 24 and 48 h or 1.9 mg/kg b.w. for 4 consecutive days. For reference mice were exposed to peanut oil (negative control) and cyclophosphamide (20 mg/kg) or ethyl methanesulfonate (EMS: 100 mg/kg) positive control for CAs and MT respectively. To analyse the effect on sperm morphology mice were exposed to single i.p. dose of 1 and 2 mg/kg b.w. of carbofuran and repeatedly to 0.5 mg/kg for 5 consecutive days. Cytogenetic analysis revealed that all the test doses induced mitotic inhibition, CAs, micronucleus (MN) formation and sperm abnormalities in a dose dependent manner. Present observations concurrent with earlier reports substantiate the genotoxic potential of carbofuran and possible risk to human beings.     

Binding of lysozyme to brush border membranes of rat kidney

The binding of ¹²⁵I-labelled egg-white lysozyme to isolated brush border membranes of rat kidney cortex was investigated. The lysozyme binding was reversible and saturable. The Scatchard plot revealed a one-component binding type with a dissociation constant of 7.8 μM and 15.6 nmol/mg membrane protein for the number of binding sites. The binding of the basic lysozyme could be reduced by basic amino acids such as l-lysine, l-ornithine or l-arginine, while neutral amino acids such as l-citrulline or l-alanine had no effect. The inhibitory effect of lysine was competitive.