Recovery of pure B-phycoerythrin from the microalga Porphyridium cruentum.

Phycoerythrin is a major light-harvesting pigment of red algae and cyanobacteria that is widely used as a fluorescent probe and analytical reagent. In this paper, B-phycoerythrin and R-phycocyanin in native state, from the red alga Porphyridium cruentum were obtained by an inexpensive and simple process. The best results of this purification procedure were scaled up by a factor of 13 to a large preparative level using an anionic chromatographic column of DEAE cellulose. Gradient elution with acetic acid-sodium acetate buffer (pH 5.5) was used. In these conditions both 32% of B-phycoerythrin and 12% of R-phycocyanin contained in the biomass of the microalgae was recovered. B-phycoerythrin was homogeneous as determined by sodium dodecyl sulfate-poly-acrylamide gel electrophoresis (SDS-PAGE), yielding three migrating bands corresponding to its three subunits, consistent with the (alpha beta)(6)gamma subunit composition characteristic of this biliprotein and the spectroscopic characterization of B-PE (UV-visible absorption and emission spectroscopy; steady-state and polarization fluorescence), is accompanied. Finally, a preliminary cost analysis of the recovery process is presented.     

Efficient and rapid purification of recombinant human alpha-galactosidase A by affinity column chromatography

The lysosomal enzyme alpha-galactosidase A (alpha-Gal A) metabolizes neutral glycosphingolipids that possess alpha-galactoside residues at the non-reducing terminus, and inherited defects in the activity of alpha-Gal A lead to Fabry disease. We describe here an efficient and rapid purification procedure for recombinant alpha-Gal A by sequential Concanavalin A (Con A)-Sepharose and immobilized thio-alpha-galactoside (thio-Gal) agarose column chromatography. Optimal elution conditions for both columns were obtained using overexpressed human alpha-Gal A. We recommend the use of a mixture of 0.9 M methyl alpha-mannoside and 0.9 M methyl alpha-glucoside in 0.1 M acetate buffer (pH 6.0) with 0.1 M NaCl for the maximum recovery of glycoproteins with multiple high-mannose type sugar chains from Con A column chromatography, and that the Con A column should not be reused for the purification of glycoproteins that are used for structural studies. Binding of the enzyme to the thio-Gal column requires acidic condition at pH 4.8. A galactose-containing buffer (25 mM citrate-phosphate buffer, pH 5.5, with 0.1 M galactose, and 0.1 M NaCl) was used to elute alpha-Gal A. This procedure is especially useful for the purification of mutant forms of alpha-Gal A, which are not stable under conventional purification techniques. A protocol that purifies an intracellular mutant alpha-Gal A (M279I) expressed in COS-7 cells within 6h at 62% overall yield is presented.     

Developing procedures for the large-scale purification of human serum butyrylcholinesterase

Human serum butyrylcholinesterase (Hu BChE) is the most viable candidate for the prophylactic treatment of organophosphate poisoning. A dose of 200 mg/70 kg is predicted to protect humans against 2× LD₅₀ of soman. Therefore, the aim of this study was to develop procedures for the purification of gram quantities of this enzyme from outdated human plasma or Cohn Fraction IV-4. The purification of Hu BChE was accomplished by batch adsorption on procainamide-Sepharose-CL-4B affinity gel followed by ion-exchange chromatography on a DEAE-Sepharose column. For the purification of enzyme from Cohn Fraction IV-4, it was resuspended in 25 mM sodium phosphate buffer, pH 8.0, and fat was removed by decantation, prior to batch adsorption on procainamide-Sepharose gel. In both cases, the procainamide gel was thoroughly washed with 25 mM sodium phosphate buffer, pH 8.0, containing 0.05 M NaCl, and the enzyme was eluted with the same buffer containing 0.1 M procainamide. The enzyme was dialyzed and the pH was adjusted to 4.0 before loading on the DEAE column equilibrated in sodium acetate buffer, pH 4.0. The column was thoroughly washed with 25 mM sodium phosphate buffer, pH 8.0 containing 0.05 M NaCl before elution with a gradient of 0.05–0.2 M NaCl in the same buffer. The purity of the enzyme following these steps ranged from 20% to 40%. The purity of the enzyme increased to >90% by chromatography on an analytical procainamide affinity column. Results show that Cohn Fraction IV-4 is a much better source than plasma for the large-scale isolation of purified Hu BChE.     

High pressure disruption: a two-step treatment for selective extraction of intracellular components from the microalga Porphyridium cruentum

The microalga Porphyridium cruentum is known to produce many components of interest. One of them is B-Phycoerythrin (B-PE), a water-soluble intracellular pigment used as an immunofluorescent probe. Current methods to extract this molecule involve total cell disruption and lead to a mix of all the water-soluble components. Subsequently, the pigment purification is very complex. An alternative approach to extract B-PE selectively and thus simplify the purification procedure has been developed using a high-pressure cell disrupter. Different pressures (from 27 to 270 MPa), extracting mediums (distilled water and original microalgae culture medium), and numbers of passages (1 to 3) have been tested. Proteins are selectively more extracted than B-PE at low pressure in original medium. It is thus possible to remove part of the intracellular proteins in a first step and then recover enriched B-Phycoerythrin fraction at higher pressure in distilled water.     

Development of a process for large-scale purification of C-phycocyanin from Synechocystis aquatilis using expanded bed adsorption chromatography

In this paper a large and scaleable method for purification of C-phycocyanin (C-PC) from the cyanobacteria Synechocystis aquatilis has been developed. Phycobiliproteins are extracted from the cells by osmotic shock and separated by passing the centrifuged cell suspension through an expanded bed adsorption chromatography (EBAC) column using Streamline-DEAE as adsorbent. The eluted C-PC rich solution is finally purified by packed-bed chromatography using DEAE-cellulose. Optimal extraction is achieved using phosphate 0.05 M buffer pH 7.0 twice. The operation of EBAC is optimized on a small scale using a column of 15 mm internal diameter (I.D.). The optimal conditions are a sample load of 4.9 mg C-PC/mL adsorbent, an expanded bed volume twice the settled bed volume and a sample viscosity of 1.020 mP. The EBAC process is then scaled up by increasing the column I.D. (15, 25, 40, 60 and 90 mm) and the success of the scale-up process is verified by determining the protein breakthrough capacity and product recovery. The yield of the EBAC step is in the range of 90-93% for every column diameter. To obtain pure C-PC, conventional ion-exchange chromatography with DEAE-cellulose is utilized and a yield of 74% is obtained. The overall yield of the process, comprising all steps, is 69%. The purification steps are monitored using SDS-PAGE and the purity of recovered C-PC is confirmed by absorption and emission spectroscopy and RP-HPLC. Results show that EBAC method is a scalable technology that allows large quantities of C-PC to be obtained without product loss, maintaining a high protein recovery while reducing both processing cost and time.     

Existence of Mg2+-dependent, neutral sphingomyelinase in nuclei of rat ascites hepatoma cells

A sphingomyelinase, which specifically hydrolyzes sphingomyelin into ceramide and phosphocholine, was solubilized from nuclear matrix fraction of rat ascites hepatoma, AH7974 cells. The solubilized enzyme was subjected to Mono Q column chromatography in an FPLC system. The sphingomyelinase which was adsorbed on the column and eluted at 0.25-0.5 M NaCl was characterized. The enzyme required 10 mM MgCl2, 0.01% Triton X-100, 1 mM dithiothreitol, and a higher concentration of buffer than 1 M for its maximal activity, and the optimal pH was 6.7-7.2 in 2 M Tris/acetic acid or 7.5 in 2 M potassium acetate/acetic acid. N-Ethylmaleimide completely inhibited the enzyme activity at 0.2 mM. Therefore, this enzyme is classified as a Mg2+-dependent, neutral sphingomyelinase. The sphingomyelinase sedimented at 4.3S through a 10-30% glycerol gradient containing 2 M potassium acetate. This enzyme was highly specific to sphingomyelin and did not hydrolyze phosphatidylcholine, phosphatidylethanolamine, phosphatidylserine, and phosphatidylinositol. Various characteristics of the nuclear sphingomyelinase were similar to those of the plasma membrane enzyme except its requirement for a high concentration of buffer and SH-reagent.     

Purification of xylanase from alkaliphilic Bacillus sp. K-8 by using corn husk column

The objective of this work was to apply low cost materials, agricultural residues, to the purification of xylanase. The results showed that crude extracellular, cellulase-free xylanase of an alkaliphilic Bacillus sp. strain K-8 could be purified in a single step by affinity adsorption–desorption on a corn husk column using a high flow rate, under the conditions 25 mM acetate buffer, pH 4.0, 4 °C, which prevented the hydrolysis of xylan by xylanase. After adsorption, the xylanase was eluted from the enzyme–corn husk complex with 500 mM Urea. The enzyme was purified 5.3-fold to homogeneity from culture supernatant. The molecular weight of the purified enzyme was 24 kDa as determined by sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS-PAGE). The specific activity and recovery yield after purification were 25.4 U/mg protein and 42.3%, respectively.     

Purification of glucose oxidase from complex fermentation medium using tandem chromatography

A fast and efficient purification method for recombinant glucose oxidase (rGOx) for flask fermentation scale (up to 2L) was designed for the purposes of characterization of rGOx mutants during directed protein evolution. The Aspergillus niger GOx was cloned into a pYES2-alphaMF-GOx construct and expressed extracellularly in yeast Saccharomyces cerevisiae. Hydrophobic interaction (HIC)/size exclusion (SEC)-tandem chromatographic system was designed for direct purification of rGOx from a conditioned complex expression medium with minimum preceding sample preparation (only adjustments to conductivity, pH and coarse filtering). HIC on Butyl 650s (50 mM ammonium acetate pH 5.5 and 1.5 M ammonium sulphate) absorbs GOx from the medium and later it is eluted by 100% stepwise gradient with salt free buffer directly into SEC column (Sephadex 200) for desalting and final polishing separation. The electrophoretic and UV-vis spectrophotometric analyses have proven enzyme purity after purification.     

Factors influencing recombinant human lysozyme extraction and cation exchange adsorption

Human lysozyme has numerous potential therapeutic applications to a broad spectrum of human diseases. This glycosidic enzyme is present in tears, saliva, nasal secretions, and milk--sources not amendable for commercial development. Recently, a high expression level of recombinant human lysozyme (0.5% dry weight) was achieved in transgenic rice seed. This paper evaluates the effects of pH and ionic strength on rice protein and lysozyme extractability, as well as their interactions with the strong cation-exchange resin, SP-Sepharose FF. The extraction conditions that maximized lysozyme yield and the ratio of extracted human lysozyme to native rice protein were not optimal for lysozyme adsorption. The conditions that gave the highest extracted lysozyme to native protein ratio were pH 4.5 and 100 mM NaCl in 50 mM sodium acetate buffer. At pH 4.5, salt concentrations above 100 mM NaCl reduced the lysozyme-to-protein ratio. The best conditions for lysozyme adsorption were pH 4.5 and 50 mM sodium acetate buffer. Lysozyme extraction and subsequent adsorption at pH 4.5 and 50 mM NaCl was an acceptable compromise between lysozyme extractability, adsorption, and purity. The primary recovery of human lysozyme from pH 6 extracts, irrespective of ionic strength, was inferior to that using pH 4.5 with unacceptably low saturation capacities and lysozyme purity. High purity was achieved with a single chromatography step by adjusting the pH 4.5 extract to pH 6 before adsorption. The disadvantage of this approach was the drastically lower saturation capacity compared to adsorption at pH 4.5.     

A simplified purification procedure for recombinant human granulocyte macrophage-colony stimulating factor from periplasmic space of Escherichia coli

Cytoplasmic expression is commonly used for production of recombinant human granulocyte macrophage-colony stimulating factor (rhGM-CSF) which most often comes with inclusion body formation. We expressed rhGM-CSF in periplasmic space of Escherichia coli and optimized its extraction by osmotic shock and purification by anion exchange chromatography. Our works show that MgCl2 at 2 mM in osmotic shock buffer improves extraction of the protein and reduces contamination with other proteins. To achieve a simplified purification procedure for rhGM-CSF, efforts were focused on the adjustment of pH of the buffers and application of proper concentration of salt. Following to measurement of the pI of 5.4 for rhGM-CSF by isoelectric focusing, the pH of dialysis buffer and buffers used in anion exchange chromatography were adjusted to 6.5 for optimal binding of the protein to the column and removal of proteins with higher pIs during washing of the column. In addition, it was found that appliance of NaCl at a concentration of 20 mM in dialysis and column washing buffers prior to elution with elution buffer containing 120 mM NaCl significantly improves purification of the protein. Starting with specific amount of total proteins obtained by osmotic shock, it was possible to recover 95% of which following to purification with a purification yield of 72% for rhGM-CSF along with appropriate biological activity.     

Hydrophobic-ionic chromatography. Its application to purification of porcine pancreas enzymes.

1. All the porcine pancreas enzymes tested, regardless of their pI's were adsorbed on Amberlite CG-50 (a weakly acidic cation exchange resin) at pH 4, where the ion-exchange group (carboxyl group) is not dissociated. The adsorption is hardly influenced by ionic strength. 2. At pH 4, the adsorbed enzymes were partially eluted by organic solvents such as 50% propanol. 3. The adsorbed enzymes were effectively eluted by increasing the pH from 4 to 6. Trypsin (pI 10.5) was eluted before carboxypeptidase A (pI 4.5 AND 5.3) WITH 0.5 M acetate buffer, whereas the former enzyme was eluted after the latter enzyme with 0.2 M 3,3-dimethyl glutarate buffer. However, with either buffer, the elution order of enzymes was not always the same as the order of the pI's. 4. By a single Amberlite CG-50 column chromatography of porcine pancreas extracts, kallikrein, carboxypeptidase B, deoxyribonuclease, carboxypeptidase A, and trypsin were purified 100-fold, 16-fmately 13%. The purification procedures included treatment with protamine, ammonium sulfate fractionation, treatment with acid, DE-32 cellulose column chromatography, gel filtration on Sephadex G-100, preparative polyacrylamide gel electrophoresis, and affinity chromatography on 5' AMP-Sepharose 4B. The last procedure, affinity chromatography on 5' AMP-Sepharose 4B, was useful for the removal of other dehydrogenases. The enzyme which was homogeneous, as shown by polyacrylamide gel electrophoresis, had a molecular weight of about 92,000. The optimum pH was at 10.0 and isoelectric point at 5.2. The enzyme accepted both L-fucose and D-arabinose as substrate, but was specific for NAD+ as coenzyme. Km values were 0.15 mM, 1.4 mM, and 0.07 mM for L-fucose, D-arabinose, and NAD+, respectively. A single enzyme catalyzed the oxidation of L-fucose and D-arabinose, which had the same configurations of hydroxyl groups from C-2 to C-4. The reaction products obtained with L-fucose as substrate were L-fucono-lactone and L-fuconic acid. The L-fucono-lactone was an immediate product of oxidation and was hydrolyzed to L-fuconic acid spontaneously. This reaction was irreversible. Therefore, it is likely that L-fucose dehydrogenase is involved in the initial step of the catabolic pathway of L-fucose in rabbit liver.     

Separation of nucleosides and nucleotides by reversed-phase high-performance liquid chromatography with volatile buffers allowing sample recovery

Reversed-phase high-performance liquid chromatography using a C18 column with volatile buffers as the eluant was applied to the separation of a number of nucleosides and nucleotides. Groups of seven nucleosides and five nucleoside monophosphates were separated isocratically employing 0.1 M trimethylammonium acetate and 2% acetonitrile at pH 7.0. Groups of seven nucleoside diphosphates and seven nucleoside triphosphates were separated with 0.1 M triethylammonium bicarbonate and 2% acetonitrile titrated to a pH of 7.1 with acetic acid. The techniques described give resolution and separations comparable to nonvolatile buffers. Moreover, the eluant trimethylammonium acetate or triethylammonium bicarbonate buffer can easily be removed in vacuo from the column effluent, making the technique useful for preparative separations of these compounds. The observed elution pattern of nucleoside phosphates suggests that "paired-ion" chromatography is involved in the separation.     

Affinity chromatography of cysteine-containing histone.

Affinity chromatography based on the reaction between SH groups in protein and +HgC6H4CO groups in the p-mercuribenzoylaminoethyl derivative of Sepharose 4B was examined with a crude preparation of calf thymus cysteine-containing histone. Adsorption of the histone onto the column by specific coupling was found to be optimal in 0.1 M citrate buffer, pH 5.5, containing 5M urea to prevent any aggregation of histones and their non-specific adsorption onto the column, and elution from the column was successfully performed by cleavage of the resulting S-Hg bond with urea-buffer solution containing 0.05 M 2-mercaptoethanol. Under these conditions both the adsorption and elution were quantitative; no adsorption was observed when either SH-blocked histone or unsubstituted Sepharose was used. The cysteine-containing histone thus recovered, after further purification by Bio-Gel P-60 chromatography to remove some cysteine-containing nonhistone proteins contaminating the starting material, showed a single band on polyacrylamide gel electrophoresis and an amino acid composition agreeing with the known sequence of this histone.     

Capture of human monoclonal antibodies from a clarified cell culture supernatant by phenyl boronate chromatography

In this work, we investigated the feasibility of using phenyl boronate (PB) chromatography for the direct capture of monoclonal antibodies from a CHO cell supernatant. Preliminary results, using pure protein solutions have shown that PB media can bind to human antibodies, not only at strong alkaline conditions but also at acidic pH values. In fact, antibodies have been found to bind in the pH range 5.5-8.5. On the other hand, insulin and human serum albumin did not bind at alkaline pH but at lower pH, which reflects the importance of non-specific interactions with the matrix. Different binding and eluting buffers were evaluated for the capture of immunoglobulin G (IgG) from a CHO cell supernatant and the most promising results were obtained using 20 mM 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid at pH 8.5 as binding buffer and 1.5 M Tris-HCl as eluting buffer. Using a step elution, all IgG was recovered in the elution pool with a maximum purification factor of 56. A gradient elution allowed a further increase of the final purity, yet achieving a slightly lower yield. IgG recovery was around 85% and the purification factor was 76. The highest purity was obtained when the pH of the cell supernatant feed was previously adjusted to 8.5. Starting from an initial protein purity of 1.1% and high-performance liquid chromatography (HPLC) purity of 2.2%, after PB adsorption, a final protein purity of 85% and a HPLC purity of 88% was achieved.     

Purification of glucosyltransferase from cell-lysate of Streptococcus mutans by counter-current chromatography using aqueous polymer two-phase system

Counter-current chromatography (CCC) using a cross-axis coil planet centrifuge (X-axis CPC) was applied to the purification of glucosyltransferase (GTF) from a cell-lysate of cariogenic bacteria. The purification was performed using an aqueous polymer two-phase system composed of 4.4% (w/w) polyethylene glycol (PEG) 8000-6% (w/w) dextran T500 containing 10mM phosphate buffer at pH 9.2 by eluting the upper phase (UP) at 1.0ml/min. The bacterial GTF in the cell-lysate of Streptococcus mutans was selectively retained in the dextran-rich lower stationary phase. The column contents were diluted and subjected to hydroxyapatite (HA) chromatography to remove the polymers from the GTF. Fractions eluted with 500mM potassium phosphate buffer were analyzed by GTF enzymatic activity as well as sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). The GTF purity in the final product was increased about 87 times as that in the cell-lysate with a good recovery rate of about 79% through this purification process.     

Basic Blue 54: a New Colorant for Monocytes

C.I. basic blue 54, a sulfur containing azo textile dye, stained the nucleus and cytoplasm of normal and leukemic monocytes bright red-violet. Essential for the staining reaction was a brief final rinse in a pH 3.6 acetic acid-sodium acetate buffer. Coloration of the type found in monocytes was not observed in other types of mature and immature leukocytes.     

Affinity purification of mouse monoclonal IgE using a protein A mimetic ligand (TG19318) immobilized on solid supports

A synthetic ligand (TG19318), deduced from the screening of a combinatorial peptide library, has been previously characterized by our group for its applicability in affinity chromatography for polyclonal and monoclonal IgG purification from crude sources. In this study we have extended the characterization of its recognition properties for other immunoglobulin classes, evaluating its ability to purify mouse monoclonal IgE from ascitic fluid. TG19318 affinity columns proved useful for a very convenient one-step purification of IgE directly from crude ascites, by loading the samples on the columns equilibrated with 50 mM sodium phosphate at pH 7 and eluting and adsorbed IgE by a buffer change to 0.1 M acetic acid. Antibody purity after affinity purification was very high and no albumin traces were detected, as determined by SDS-PAGE analysis. Antibody activity was fully recovered after purification, as determined by immunoassays on antigen-coated plates, and up to 5 mg of IgEs could be purified on a 1 ml column in a single run.     

High pressure liquid chromatography solvent systems for studies of bile acid biosynthesis

Reversed phase high pressure liquid chromatography (HPLC) solvent systems have been developed for the separation of intermediates in the formation of bile acids and bile acid conjugates from cholesterol. Four different mobile phases (water-methanol, 10 mM acetate buffer (pH 4.37)-methanol, 30 mM trifluoroacetic acid (pH 2.9 with triethylamine)-methanol, and 50 mM potassium phosphate buffer (pH 7.0)-2-propanol) have been applied to obtain separation of all the main intermediates with use of the same reversed phase column (Zorbax ODS).     

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.     

Affinity Purification of Synenkephalin-Containing Peptides Including a Novel 23.3-Kilodalton Species

Abstract: Affinity chromatography has been used for rapid and high-yield purification of synenkephalin (proenkephalin 1 -70) containing peptides present in bovine adrenal medulla (BAM) chromaffin granular lysate. A column of CN-Br-activated Sepharose 4B coupled to synenkephalin antiserum bound synenkephalin immunoreactivity which was eluted by a stepwise gradient of 50 mM ammonium acetate containing 20% (vol/vol) acetonitrile over the pH range 7–3. Synenkephalin immunoreactivity emerged as two peaks, eluting at pH 5.5 and 4.5. Characterization of the two peaks by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and immunoblotting indicated that the pH 5.5 peak contained principally low-molecular-weight proenkephalin species (8.6 and 12.6 kilodaltons), whereas the pH 4.5 peak contained, in addition, high-molecular-weight proenkephalin species (18.2 and 23.3 kilodaltons). The 8.6- and 12.6- kilodalton species were isolated from the pH 5.5 peak by TSK gel filtration HPLC, whereas the pH 4.5 peak was further purified by passage over successive affinity columns coupled to antiserum against BAM 22P (proenkephalin 182–203) and [Met⁵]-enkephalin-Arg⁶-Gly⁷-Leu⁸. The former column retains the 23.3-kilodalton species, whereas the latter column retains the 18.2-kilodalton species. The 23.3- kilodalton peptide represents a novel putative proenkephalin intermediate (proenkephalin-1–206), containing [Leu⁵]- enkephalin at the C-terminus.