Quantitative comparison on the refinement of horse antivenom by salt fractionation and ion-exchange chromatography

A quantitative comparison was made on the fractionation of pepsin-digested horse antivenoms by ammonium sulfate (AS) fractional precipitation and ion-exchange chromatography on Q-Sepharose. In the precipitation process, pepsin digested horse anti-Naja kaouthia serum was precipitated by 30% saturated AS followed by 50% saturated AS. The recovery of antibody activity [as measured by an enzyme-linked immunosorbent assay (ELISA) against the cobra postsynaptic neurotoxin 3] from the 30–50% saturated AS precipitate was 53% with a 1.93-fold purification. For the chromatographic process, the behavior of the horse antitoxin antibody and its F(ab′)₂ fragments was first studied. The pepsin digested horse serum was then desalted on a Bio-gel P-2 column followed by chromatography on Q-Sepharose using a linear gradient (20 mM Tris-HCl, pH 8.0 containing 0.0 to 0.5 M NaCl). A peak containing primarily the F(ab′)₂ antibody could be obtained. This peak constituted 73% of the total antivenom activity with 2.08-fold purification. The total recovery of antibody activity by the chromatographic process was 90%. The yield of antibody activity was about 2-fold higher than that reported previously with other fractionation procedures. The implications of these results for the refining of horse therapeutic antivenoms are discussed.     

Comparative evaluation of three purification methods for the nucleocapsid protein of Newcastle disease virus from Escherichia coli homogenates

In the present study, the performances of conventional purification methods, packed bed adsorption (PBA), and expanded bed adsorption (EBA) for the purification of the nucleocapsid protein (NP) of Newcastle disease virus (NDV) from Escherichia coli homogenates were evaluated. The conventional methods for the recovery of NP proteins involved multiple steps, such as centrifugation, precipitation, dialysis, and sucrose gradient ultracentrifugation. For the PBA, clarified feedstock was used for column loading, while in EBA, unclarified feedstock was used. Streamline chelating immobilized with Ni2+ ion was used as an affinity ligand for both PBA and EBA. The final protein yield obtained in conventional and PBA methods was 1.26% and 5.56%, respectively. It was demonstrated that EBA achieved the highest final protein yield of 9.6% with a purification factor of 7. Additionally, the total processing time of the EBA process has been shortened by 8 times compared to that of the conventional method.     

Simplified purification of equine chorionic gonadotropin (eCG)––an example of the use of magnetic microsorbents for the isolation of glycoproteins from serum

Classical purification of the glycoprotein equine chorionic gonadotropin (eCG) from serum includes pH fractionation with metaphosphoric acid, two ethanol precipitation steps as well as dialysis followed by fixed-bed chromatography. A simplified process requiring only 1/3 of the solvent and improving the yield from 53 to 65% has been developed. The process comprises an ultra-/diafiltration step after the first ethanol precipitation, directly followed by an adsorption/desorption procedure based on magnetic microadsorbents with N,N-diethyl-ammonium functionalization. The process reaches an overall purification factor of eCG of more than 1800 and an average product activity of 1300 IU_ELISA/mg. After adapting the parameters of the fractionation and the type of magnetic microadsorbents, the new concept is likely to be transferable to other serum proteins.     

Quantifying process tradeoffs in the operation of chromatographic sequences

A method for the rapid representation of key process tradeoffs that need to be made during the analysis of chromatographic sequences has been proposed. It involves the construction of fractionation and maximum purification factor versus yield diagrams, which can be completed easily on the basis of chromatographic data. The output of the framework developed reflects the degree of tradeoff between levels of yield and purity and provides a fast and precise prediction of the sample fraction collection strategy needed to meet a desired process specification. The usefulness of this approach for the purposes of product purification and contaminant removal in a single chromatographic step has been successfully demonstrated in an earlier paper and it is now extended by application to a chromatographic sequence: the separation of a hypothetical three-component protein system by hydrophobic interaction chromatography (HIC) followed by size exclusion chromatography (SEC). The HIC operation has a strong impact upon the subsequent SEC step. The studies show how the analysis of performance in such a chromatographic sequence can be carried out easily and in a straightforward fashion using the fractionation diagram approach. The methodology proposed serves as a useful tool for identifying the process tradeoffs that must be made during operation of a sequence of chromatographic steps and indicates the impact on further processing of the cut-point decisions that are made.     

Evaluation of the effects of the parameters involved in the purification of clavulanic acid from fermentation broth by aqueous two-phase systems

The purification of clavulanic acid (CA), which is an important β-lactam antibiotic produced by submerged cultivation of Streptomyces clavuligerus, was studied through the use of phosphate and polyethylene glycol-based aqueous two-phase systems. The parameters’ effect on the yield and purification was evaluated through an experimental design and the preliminary results showed that the polyethylene molecular mass and tie-line length and phase volume ratio exerted the strongest effect on the yield and distribution coefficient in the range tested. In addition, the response surface methodology was used to optimize the distribution coefficient, yield, and purification factor. The optimal conditions of yield and purification factor are in the regions where polyethylene has a low molecular mass, pH close to the isoelectric point, and lower top phase volume. A 100% yield and a 1.5-fold purification factor are obtained when extracting CA by maximizing the conditions of an aqueous two-phase system.     

Recovery of endo-polygalacturonase using polyethylene glycol-salt aqueous two-phase extraction with polymer recycling

The partitioning behaviour of endo-polygalacturonase (endo-PG) and total protein from a clarified Kluyveromyces marxianus fermentation broth in polyethylene glycol (PEG)-ammonium sulfate and PEG-potassium phosphate (pH=7) aqueous two-phase systems was experimentally investigated. Both the enzyme and total protein partitioned in the bottom phase for these two kinds of systems. The enzyme partitioning coefficient can be lower than 0.01 in PEG8000-(NH₄)₂SO₄ ATPS with a large phase volume ratio and a moderate tie-line length, which implies the possibility of concentration operation using aqueous two phase partitioning. An ion-exchange separation of high purification efficiency was applied to analyze the clarified and dialyzed fermentation broth. A total purification factor of only 2.3 was obtained, which indicated the high enzyme protein content in the total protein of the fermentation broth. Consequently, the main purpose for separating endo-PG is concentration rather than purification. A separation scheme using an aqueous two-phase extraction process with polymer recycling and a dialysis was proposed to recover endo-PG from the fermentation supernatant of K. marxianus for commercial purpose. A high enzyme recovery up to 95% and a concentration factor of 5 to 8 with a purification factor of about 1.25 were obtained using the single aqueous two-phase extraction process. More than 95% polymer recycled will not affect the enzyme recovery and purification factor. Dialysis was used mainly to remove salts in the bottom phase. The dialysis step has no enzyme loss and can further remove small bulk proteins. The total purification factor for the scheme is about 1.7.     

Effective method of simultaneous isolation from human serum of highly purified factors B and D of the alternative pathway of complement activation

A simple method for isolation from human serum of the complement alternative pathway factor B, in a yield over 40% and purity over 80% with respect to protein, has been developed. Such a high yield was reached due to rejection of ammonium sulphate fractionation and employment of only two chromatographic stages: on CM-Sephadex C-50 and on DEAE-Sepharose CL-6B. An additional chromatography on QAE-Sephadex A-50 provides factor B of 100% purity but with a loss of some amount of protein (yield approximately 20%). One of the fractions, obtained at the first stage of factor B purification, contained also factor D. After rechromatography on CM-Sephadex C-50 and gel filtration on Sephadex G-75 it afforded factor D in yield more than 60% and purity above 100%.     

Isolation, Purification, and Crystallization of Aspartate Aminotransferase from Wheat Grain

A procedure for isolation and purification of aspartate aminotransferase from wheat grain includes chromatography on DEAE cellulose, acidification-alkalization, precipitation with protamine sulfate, fractionation with ammonium sulfate, and chromatography on hydroxyapatite. The yield of protein was 27% with 95% purity. Crystals of the enzyme (0.05 x 0.025 x 0.015 mm3) were obtained from ammonium sulfate solution.     

Caprylic acid precipitation method for impurity reduction: An alternative to conventional chromatography for monoclonal antibody purification

We report the use of caprylic acid based impurity precipitation as (1) an alternative method to polishing chromatography techniques commonly used for monoclonal antibody purification and (2) an impurity reduction step prior to harvesting the bioreactor. This impurity reduction method was tested with protein A purified antibodies and with cell culture fluid. First, the operational parameters influencing precipitation of host cell proteins and high molecular weight aggregate in protein A pools were investigated. When used as a polishing step, the primary factor affecting purification and yield was determined to be pH. Caprylic acid precipitation was comparable to polishing IEX chromatography in reducing host cell protein and aggregate levels. A virus reduction study showed complete clearance of a model retrovirus during caprylic acid precipitation of protein A purified antibody. Caprylic acid mediated impurity precipitation in cell culture showed that the impurity clearance was generally insensitive to pH and caprylic acid concentration whereas yield was a function of caprylic acid concentration. Protein A purification of caprylic acid precipitated cell culture fluid generated less turbid product pool with reduced levels of host cell proteins and high molecular weight aggregate. The results of this study show caprylic acid precipitation to be an effective purification method that can be incorporated into a production facility with minimal cost as it utilizes existing tanks and process flow. Eliminating flow through chromatography polishing step can provide process intensification by avoiding the process tank volume constraints for high titer processes. Biotechnol. Bioeng. 2012; 109: 2589–2598. © 2012 Wiley Periodicals, Inc.     

Chromatography in plasma fractionation: benefits and future trends

Industrial-scale chromatographic fractionation and purification methods have been used increasingly in the last few years for plasma fractionation. This has resulted in the development of a new generation of therapeutic plasma derivatives, especially coagulation factors, protease inhibitors and anticoagulants. Implementation and combination of ion-exchange, affinity and size-exclusion chromatography have allowed the development of new therapeutic products with improved purity and safety for treating congenital or acquired plasma protein deficiencies in patients. More recently, the benefit of chromatographic purification of plasma proteins in the removal of plasma-borne viruses has been revealed. Development of packing materials with improved characteristics for industrial applications, including higher capacity and rigidity, should further promote the use of chromatography as an essential plasma fractionation tool and confine more and more the traditional ethanol precipitation methods to the final processing stages used to recover albumin.     

Purification of human erythropoietin.

Human erythropoietin, derived from urine of patients with aplastic anemia, has been purified to apparent homogeneity. The seven-step procedure, which included ion exchange chromatography, ethanol precipitation, gel filtration, and adsorption chromatography, yielded a preparation with a potency of 70,400 units/mg of protein in 21% yield. This represents a purification factor of 930. The purified hormone has a single electrophoretic component in polyacrylamide gels at pH 9, in the presence of sodium dodecylsulfate at pH 7, and in the presence of Triton X-100 at pH 6. Two fractions of the same potency and molecular size, by sodium dodecyl sulfate gel electrophoresis, but differing slightly in mobility at pH 9, were obtained at the last step of fractionation. The nature of the difference between these two components is not yet understood.     

Partial purification and characterization of the low density lipoprotein receptor from bovine adrenal cortex

The low density lipoprotein (LDL) receptor has been solubilized from bovine adrenocortical membranes with octyl-beta-D-glucoside and purified 350-fold in the presence of the detergent. The activity of the solubilized receptor was assayed by precipitating the receptor with acetone in the presence of egg phosphatidylcholine liposomes. the receptor-phosphatidylcholine liposomes bound 125I-LDL with the same affinity and specificity as did the native LDL receptor of intact membranes. The complex of receptor and octylglucoside had a Stokes radius of 53.5 A as determined by agarose gel filtration. The sedimentation coefficient, s20,w, of the receptor . octylglucoside complex was 7.3 as determined by metrizamide density gradient centrifugation. An identical value for the sedimentation coefficient was obtained when deuterium oxide was substituted for water in the metrizamide gradient. These data were used to derive an estimate of 163,000 for the molecular weight of the LDL receptor . octylglucoside complex (range of molecular weight, 152,000 to 170,000). The receptor is an acidic protein as determined by its behavior on ion exchange chromatography. In the most highly purified LDL receptor preparation, which had been subjected to the sequential steps of solubilization, DEAE-cellulose chromatography, agarose gel filtration, and phosphatidylcholine/acetone precipitation, the receptor was estimated to constitute about 5% of the total protein. Thus, complete purification of the LDL receptor from bovine adrenocortical membranes will require an additional 20-fold purification, or a total purification of about 7,000-fold.     

Isolation of a Pure Dextranase from Penicillium funiculosum

A dextranase, produced by Penicillium funiculosum, was purified 1,000-fold to yield the enzyme which was demonstrated by gel electrophoresis and electrofocusing to be a homogeneous protein. The purification method included acetone partition, ammonium sulfate fractionation, gel filtration, iron defecation and precipitation, and diethylaminoethyl-cellulose chromatography. The pure enzyme was also obtained by preparative gel electrophoresis. Gel-permeation chromatography indicates a molecular weight of 41,000. An isoelectric pH of 4.6 was established by electrofocusing. A 1-mg amount of the enzyme hydrolyzes a dextran substrate to yield 27,000 isomaltose reducing units in 2 hr.     

Isolation and sequence of tryptic peptides from the proton-pumping ATPase of the oat plasma membrane

In crude extracts of plant tissue, the M_r = 100,000 proton-pumping ATPase constitutes less than 0.01% of the total cell protein. A large-scale purification procedure is described that has been used to obtain extensive protein sequence information from this enzyme. Plasma membrane vesicles enriched in ATPase activity were obtained from extracts of oat roots by routine differential and density gradient centrifugation. Following a detergent wash, the ATPase was resolved from other integral membrane proteins by size fractionation at 4°C in the presence of lithium dodecyl sulfate. After carboxymethylation of cysteine residues and removal of detergent, the ATPase was digested with trypsin and resultant peptide fragments separated by reverse phase high performance liquid chromatography. Peptides were recovered with high yield and were readily sequenced by automated Edman degradation on a gas-phase sequencer. Of the eight peptides sequenced, six showed strong homology with known amino acid sequences of the fungal proton-pumping and other cation-transporting ATPases.     

Purification of IgG and albumin from human plasma by aqueous two phase system fractionation

The current shortages in human plasma products at global levels justify the development of new, cost effective plasma fractionation methods. We have developed a fractionation process to obtain immunoglobulin G (IgG) and albumin‐enriched fractions based on polymer‐salt aqueous two phase system (ATPS). A small‐scale (0.02 L) ATPS composed of polyethyleneglycol 3350 (PEG), potassium phosphate and sodium chloride, at pH 6.1, was evaluated and subjected to 50‐fold scale‐up (1 L). Further purification of the fractions was performed using caprylic acid precipitation and ion exchange chromatography. Similar yield and purity were obtained at both small and large scales. IgG precipitated in the PEG rich upper phase at 83% recovery and 2.75‐fold purification factor. An 81% pure albumin fraction was obtained in the salt rich bottom phase with a 91% yield. After polishing, IgG was obtained at a recovery of 70% and a purity of 92%. Corresponding values for albumin were 91% and 90%. This IgG and albumin fractionation technology deserves further evaluation as it may represent a potential alternative to conventional plasma fractionation methods. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 28: 1005–1011, 2012     

A simple purification procedure of biologically active recombinant human granulocyte macrophage colony stimulating factor (hGM-CSF) secreted in rice cell suspension culture

A simple purification procedure of bioactive human granulocyte macrophage colony stimulating factor (hGM-CSF) secreted in rice cell suspension culture has previously been described. In this study the protein was purified to apparent homogeneity with an overall yield of 80.1% by ammonium sulfate precipitation and a single chromatographic step involving FPLC-anion exchange chromatography. The purified hGM-CSF revealed at least five glycosylated forms ranging from 21.5∼29 kDa, and its biological activity was independent of the glycosylation pattern. This is the first purification report of recombinant hGM-CSF to apparent homogeneity from rice cell suspension cultures.     

Tyroslyl-tRNA synthetase from baker's yeast. Rapid isolation by affinity elution, molecular weight of the enzyme, and determination of essential sulfhydryl groups.

Tyrosyl-tRNA synthetase (EC 6.1.1.1) has been isolated from baker's yeast with an overall purification factor of more than 5000. After opening the cells, pH 4.8 precipitation, ammonium sulfate fractionation, removal of the nucleic acids with DEAE-cellulose and chromatography on CM-Sephadex, the critical purification step is the elution of the cation-exchanger-bound tyrosyl-tRNA synthetase with tRNATyr. The homogeneous enzyme exhibits a molecular weight of 40 000 as estimated by sedimentation equilibrium centrifugation and dodecylsulfate-gel electrophoresis under reducing and non-reducing conditions. Gel filtration experiments show a molecular weight of about 100 000 indicating the existence of an active dimeric form. The possibility of proteolytic cleavage of the enzyme is excluded. The reaction of tyrosyl-tRNA synthetase with p-chloromercuribenzoate and N-ethylmaleimide reveals two repidly reacting sulfhydryl groups per subunit of molecular weight 40 000, as demonstrated by the inhibition of aminoacylation and the isolation of enzyme-inhibitor complexes. In addition an efficient purification method is described for isolating tRNATyr from soluble ribonucleic acid from baker's yeast in three chromatographic steps in a yield of 28%.     

Development and optimization of fractional precipitation for the pre-purification of (+)-dihydromyricetin

A novel fractional precipitation process, both simple and efficient, was developed for producing (+)-dihydromyricetin in high purity and high yield from crude extracts. The optimal acetone composition in water, initial (+)-dihydromyricetin concentration in crude extract, storage temperature, storage time, and pH were 1/5 (v/v), 0.1 g/mL, 4°C, 32 h, and 9.0, respectively. Crude extracts were efficiently pre-purified using fractional precipitation of (+)-dihydromyricetin by differences of solubility in an acetone solution, increasing purity from 55.0 to over 84.9% with an overall yield of 97.5%. The use of fractional precipitation for pre-purification allowed for rapid and efficient separation of (+)-dihydromyricetin from interfering compounds and dramatically increased the purity of crude (+)-dihydromyricetin for subsequent purification steps.     

Phosphoprotein Phosphatase of Soybean Hypocotyls: PURIFICATION, PROPERTIES, AND SUBSTRATE SPECIFICITIES

A soybean histone-type protein kinase was used to prepare ³²P-labeled histone H1 as substrate for purification and characterization of a phosphoprotein phosphatase (EC 3.1.3.16) from soybean hypocotyls. The phosphatase has been purified 169-fold by ammonium sulfate fractionation, ethanol precipitation, and chromatography on Sephadex G-150, DEAE-Sephadex A-25 and Sephadex G-100. The activity of the phosphoprotein phosphatase is distinct from that of acid and alkaline phosphatases (EC 3.1.3.1) as well as from that of nucleotidases. The final enzyme preparation does not contain histone protease activity, although it can be detected during the early stages of purification. The protease(s) apparently can attack phosphorylated histone H1, indicating that phosphorylation does not protect the protein against proteolytic degradation.     

Manual N-terminal microsequencing of proteins electroeluted from polyacrylamide gel slices

A simple and rapid procedure for preparation of proteins for manual microsequencing using sodium dodecyl sulfate gel electrophoresis is described. The procedure involves pre-electrophoretic labeling of the protein amino groups with a coloured Edman reagent, disk electrophoresis for purification or fractionation of the proteins, and reversed electrophoretic transfer of the separated protein from gel slices into a small volume of buffer (100 to 150 microliter) using a discontinuous conductivity gradient to recover the proteins. The pre-electrophoretic labeling facilitates location of the separated proteins in the gel and the monitoring of their complete electroelution. The isolated proteins are separated from excess of salts by acetone precipitation and solvent partitioning in pyridine/water (1:1) and subjected to manual DABITC/PITC degradation.