Elisabeth Wenisch

Preparative protein purification in a multi-compartment electrolyser with immobiline membranes

Abstract Preparative electrophoresis in gel phases, including isoelectric focusing, is characterized by low load limits (only a few milligrams of protein per millilitre of matrix), low recoveries (rarely exceeding 70%) and heavy contamination from neurotoxic gel material (unreacted monomers and ungrafted oligomers). A multi-compartment electrolyser is described based on the principle of highly buffering Immobiline membranes of well defined isoelectric points (pI). Each chamber is delimited by isoelectric membranes having pIs encompassing the pI value of the components of interest in the mixture to be separated. Such components are transported electrophoretically from chamber to chamber until they collect in the chamber defining their pI values. As the sample feed is kept in a number of reservoirs equal to the number of chambers in the electrolysers, at the end of the purification process each reservoir will contain, under ideal conditions, a homogeneous protein fraction. Examples of the purification of r-DNA Eglin C and of monoclonal antibodies are given.

Preparative purification of human monoclonal antibody isoforms in a multi-compartment electrolyser with immobiline membranes

The performance of a multi-compartment electrolyser with isoelectric Immobiline membranes for large-scale protein purification is evaluated. Owing to the presence of isoelectric membranes possessing a high buffering capacity and ionic strength, isoelectric protein precipitation inside the membranes, one of the major drawbacks of present membrane uses, is fully avoided. In addition, owing to this novel membrane technology, pH gradient decay, typical of isoelectric focusing in carrier ampholytes, is fully eliminated and pH and conductivity constancy is guaranteed in all flow chambers for running periods of more than 11 days (160,000 V h). The membranes described possess a unique selectivity, in that they act by modulating the surface charge (i.e., the mobility) of macroions crossing or tangential to them. The concept of isoelectric Immobiline membranes acting like a pH-stat unit is introduced. Protein homogeneity in each chamber of the electrolyser can be achieved even when purifying human monoclonal antibodies against HIV-1, which possess high pI values (9.0-9.6), are large molecules (Mr 150,000) and are fractionated in the presence of large micelles of neutral detergents.

Comparison of protein A, protein G and copolymerized hydroxyapatite for the purification of human monoclonal antibodies

Protein A Superose, protein G Sepharose fast flow and copolymerized hydroxyapatite were used for the purification of human monoclonal antibodies against HIV 1. Both desalted culture supernatant and a prepurified protein solution were used as starting materials. The different runs were compared with respect to yield and recovery of biological activity. The biological activity (specific reactivity) was checked by antigen enzyme-linked immunosorbent assay with recombinant antigen. The human monoclonal antibodies could not be selectively eluted from the hydroxyapatite but elution could be effected from the protein A Superose at pH 4.0 and from protein G at pH 3.0. The eluted immunoglobulin G was distributed over a broad pH range when protein G Superose was used. Biologically active material could be obtained from protein A Superose and protein G Sepharose fast flow.

Protein purification in multicompartment electrolyzers with isoelectric membranes

Preparative purification of proteins under isoelectric conditions is reviewed, with particular regard to novel equipment, a multicompartment electrolyzer with isoelectric membranes, which can capture any desired protein into an isoelectric trap as the sole, ultra-pure component. This novel machine is based on the Immobiline chemistry, i.e. the novel generation of non-amphoteric buffers, based on the chemistry of acrylamides, which can be insolubilized onto polyacrylamide supports. After a description of the instrument and of its performance, a number of protein purification protocols are described, leading to truly homogeneous (by the most stringent criterion of surface charge) protein fractions. Such a high charge purity has been found to be often a fundamental prerequisite for the growth of protein crystals. Interfacing the electrolyzer with mass spectrometry has permitted the decoding of the structure of minor components generated from a parental molecule, especially ones having a higher pI. It was found that these species were often generated either by proteolytic cleavage or by the formation of a trisulphide bridge between two Cys residues. A unique application of the electrolyzer is finally described: its use as an immobilized enzyme reactor under an electric field. The performance of this reaction is outstanding, in that the kinetic parameters of the immobilized enzyme are identical to those of a free enzyme form.

Pilot scale production of a human monoclonal antibody against human immunodeficiency virus HIV-1

Human monoclonal antibodies against the transmembrane protein gp41 of HIV-1 were isolated and purified on a pilot scale. A purification scheme was established for the production of human monoclonal antibodies on the gram scale. 50 1 of culture supernatant can be treated in one purification cycle. The hybridomas were mass cultured in an airlift fermenter. The culture broth was clarified by microfiltration and chromatographed on CM-Sepharose fast flow and protein A Superose. Scale up of the high performance affinity chromatography from 1 ml protein A Superose up to 40 ml is described. All desalting steps were performed by gel filtration on Sephadex G-25 coarse. The yield of the whole purification procedure is in the range of 50-60%. The purity is higher than 99.9%. DNA and reverse transcriptase could not be detected. The whole method is designed as a basis for scale up to industrial scale. Results from quality control assays have proven the validity of this approach.

Isoelectric focusing in a multicompartment electrolyzer with zwitterionic membranes, exemplified by purification of glucoamylase.

A highly purified preparation of glucoamylase G1 from Aspergillus niger was found, by isoelectric focusing in immobilized pH gradients, to contain a major form with a pI of 3.50 and a number of minor, more acidic and more basic contaminants. The major isoform was purified to homogeneity by recycling isoelectric focusing in a multicompartment electrolyzer, by confining this form in between two zwitterionic membranes, with pI 3.49 at the anodic side and pI 3.52 at the cathodic side. Recoveries were high (90%) and, notwithstanding the rather low operational pH, the electrosmotic flow was minimal and no protein precipitation occurred up to concentrations of 2.5 mg/ml (at the isoelectric point). The forms resolved in an analytical focusing gel were subjected to two types of in situ enzyme detections, by the glucose oxidase peroxidase (GOP) test and by the starch-iodine test. By both criteria all resolved zones exhibited enzyme activity, the GOP assay, however, following more closely the Coomassie blue stained protein profile. By computer modelling, it is shown that it is impossible to obtain linear pH gradients at such low pH values (pH 2.5-4.5 intervals) when the mixture has a low buffering power (beta = 2.0 mequiv.l-1 pH-1). When the beta power was gradually raised (beta = 4, beta = 6, beta = 8) the pH gradient became progressively linear until, in a recipe with beta = 10 mequiv.l-1 pH-1 full linearity of the pH gradient could be obtained. This is shown to be due to the substantial buffering power of bulk water in the pH 2.5-3.5 region.

Crystallization of the Fab from a human monoclonal antibody against gp 41 of human immunodeficiency virus type I.

A monoclonal IgG antibody directed against gp 41 from the human immunodeficiency virus (HIV-1) has been crystallized in both intact and Fab forms. Crystals of the intact antibody grow as tetragonal-like prisms too small for conventional X-ray analysis. However, the Fab portion of the antibody produces suitable plate-like crystals which belong to the space group P2(1)2(1)2(1) with unit cell constants of a = 66.5 A, b = 74.3 A and c = 105.3 A. There is one molecule of Fab in the asymmetric unit. The Fab crystals show diffraction to d-spacings less than 3.0 A.

Isolation of human monoclonal antibody isoproteins by preparative isoelectric focusing in immobilized pH gradients

A method for preparative isolation of human monoclonal antibody isoproteins is described in the present paper. A human monoclonal antibody directed against the transmembrane protein gp 41 from the human immunodeficiency virus (HIV-1) was used in this study. The antibody belongs to the IgG1 subtype and exhibits antibody dependent cellular cytotoxicity. The resolving power of conventional preparative protein separation techniques such as ion-exchange chromatography, chromatofocusing and lectin affinity chromatography is too poor for a complete separation of isoproteins. The more sophisticated technique of chromatofocusing on FPLC-based material (Mono P, Pharmacia) did not satisfy our expectation. With semipreparative IEF in immobilized pH gradients we were able to prepare the different isoproteins of a human monoclonal antibody in milligram amounts. No significant difference between the single isoproteins with respect to specificity and avidity to the recombinant antigen (rec gp 160) was detected. Therefore, we assume that the separation conditions did not influence the immunochemical nature of the antibody and significant denaturation and/or precipitation of the IgG did not occur. Furthermore the method affords preparative separation with resolution equivalent to analytical runs. Experiments for scale up and further characterization of isoproteins (carbohydrate composition, amino acid analysis, half life times etc.) are in progress.

Capillary zone electrophoresis for monitoring r-DNA protein purification in multi-compartment electrolysers with immobiline membranes

Isoforms of human monoclonal antibodies against the gp-41 of AIDS virus and of human recombinant superoxide dismutase have been purified to homogeneity by isoelectric focusing (IEF) in a multi-compartment electrolyser with isoelectric, immobiline membranes. This system allows the processing of large sample volumes and gram-scale protein loads and can resolve isoforms as close as 0.001 in pI difference. The purification progress was usually monitored by analytical IEF in immobilized pH gradients (IPG). Capillary zone electrophoresis (CZE) was applied to the monitoring of the content of each chamber of the electrolyser. CZE was found to be superior in terms of speed of analysis and quantification (but only by UV reading at 200-210 nm, i.e., in the region of the peptide bond) but, notwithstanding the millions of theoretical plates reported, was no match for the resolving power of IPGs, at least for protein analysis. When compared also with chromatofocusing, the resolving power decreases in the order IPG greater than CZE much greater than chromatofocusing.

Isoelectric precipitation and gel chromatography for purification of monoclonal IgM

A preparative scale purification procedure of monoclonal IgM from hybridoma culture supernatant with high protein content is described. The procedure consists of three steps starting with ultrafiltration followed by isoelectric precipitation and gel chromatography. Cells and debris from culture supernatant were removed by microfiltration. The clarified supernatant was concentrated 400-fold in a hollow fibre ultrafiltration apparatus (cut off 100 000 daltons). The concentrate was titrated with dilute histidine/HCl buffer close to the isoelectric point of the IgM. Precipitated proteins were harvested by centrifugation, washed and redissolved. The protein fraction containing the IgM was further purified by gel chromatography on a Sephacryl S300 column. This procedure leads to product recovery of 40% and purity of 99% related to total protein.