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P R Levison

Publications and source records attributed to P R Levison.

17 recordsLinked to original sources
PubMed2001

Direct isolation of monoclonal antibodies from tissue culture supernatant using the cation-exchange cellulose Express-Ion S.

The chromatography of the murine hybridoma cell C595/102 culture supernatant expressing the therapeutic monoclonal antibody C595, on the cation-exchange cellulose Whatman Express-Ion Exchanger S has been investigated. Initial method scouting studies using purified C595 in 1-ml mini columns demonstrated that binding capacity and binding efficiency were dependent not only on decreasing pH but also on the buffer salts used to prepare the mobile phase. Under optimised conditions of 0.1 M sodium acetate buffer, pH 5.0, we were able to separate purified C595 from BSA, the major contaminant in tissue culture fluid. Under these conditions immunoreactive C595 could be isolated directly from tissue culture supernatant. A scale-down study was carried out using a 25-ml column operated at a flow-rate of 150 cm/h which also yielded purified immunoreactive antibody. This procedure should now be suitable for scale-up.

Animals↗
PubMed2001

Performance comparison of suspended bed and batch contactor chromatography.

In some applications, the purification and recovery of biomolecules is performed via a cascade of batch adsorption and desorption stages using agitated contactors and related filtration devices. Suspended bed chromatography is a recent process-scale innovation that is applicable to these separations. This hybrid technique exploits the benefits of combining batch adsorption in an agitated contactor with elution in an enclosed column system. To some extent, the process is similar to batch contactor chromatography but can be fully contained and significantly quicker. The process has two steps; first the fluid containing the sample is mixed with the adsorbent in a stirred tank. Second, the slurry suspension is transferred directly into a specialized column, such as an IsoPak column. The media with the adsorbed product is formed as a packed bed, whilst the suspension liquid is passed out of the column. The product is then eluted from the packed bed utilizing standard column-chromatography techniques. The performance of the suspended bed and the agitated contactor operations are demonstrated both by full-scale experimental results and process simulations. The purification of ovalbumin from a hen-egg white feedstock by anion-exchange chromatography was used as a case study in order to prove the concept. With the availability of both pump-packed systems and shear-resistant media, suspended bed chromatography is a better alternative for a range of applications than the traditional batch separations using agitated contactors.

Adsorption↗
PubMed2000

Suspended bed chromatography, a new approach in downstream processing.

A new technique in downstream processing, suspended bed chromatography has been developed. This hybrid technique exploiting the benefits of batch adsorption and the process advantages of an enclosed column system can be carried out using established contactors and adsorbents. A 44 cm I.D. IsoPak column and the anion-exchange cellulose Express-Ion Exchanger Q were used in the purification of ovalbumin from hen-egg white. After suspension of 16.25 kg Express-Ion Q in 500 l of feedstock containing 5 g protein/l, adsorption was effected by recirculation of the suspension using the IsoPak slurry preparation station. Protein-loaded adsorbent was collected in the IsoPak column unit, where it was washed and protein desorbed using gradient elution at a flow-rate of 300 cm/h. The entire process was complete in under 3 h. With the introduction of pump-packed column systems and the availability of mechanically strong adsorbents suitable for column separations, suspended bed chromatography offers a new approach to downstream processing and provides a less challenging alternative to batch separations.

Adsorption↗
PubMed1999

Influence of column design on process-scale ion-exchange chromatography.

The performance of two new designs of pump-packed axial flow process chromatography columns have been evaluated for the preparative anion-exchange chromatography of hen egg-white proteins using Whatman Express-Ion Exchanger Q. A 16 1 Side-Pack column and a 24 1 IsoPak column containing Express-Ion Q were used in this study. In each case ca. 20 1 feedstock containing 5-7 g protein/l, was applied per litre packed bed at flow-rates of ca. 150 and 300 cm/h. In each case the ovalbumin binding capacity was ca. 70 g/l packed bed with ca. 100% (w/w) recovery of applied protein. A clean-in-place procedure involving storage in 0.5 M NaOH was effective in maintaining chromatographic performance in all cases. These data were consistent with our previous work using the more traditionally configured slurry-packed axial flow columns. Each of these column designs were easy to use facilitating rapid packing with this adsorbent and in the case of IsoPak rapid pump unpacking. The introduction of these column designs significantly improves the task of column packing, hitherto a labour intensive, physically demanding and potentially unreproducible process.

Animals↗
PubMed1998

New approaches to the isolation of DNA by ion-exchange chromatography.

The performance of different anion-exchange media have been compared for the isolation of plasmid DNA and genomic DNA from bacterial cells and human whole blood. Whatman DEAE-Magarose, based on an agarose bead containing a paramagnetic component, has been compared with prepacked gravity-flow columns containing a derivatised silica matrix. In each case the DNA isolation at various scales of operation was similar both in terms of yield and quality. The magnetic susceptibility of DEAE-Magarose is very high, facilitating the use of this separation technique for rapid flexible batch chromatographic processes, a limitation of the prepacked column techniques.

Chromatography, Ion Exchange↗
PubMed1998

Recent developments of magnetic beads for use in nucleic acid purification.

The performance of Magarose, an agarose-based bead containing a paramagnetic component has been evaluated. The anion exchanger DEAE-Magarose is effective at binding DNA from a crude cell lysate. The plasmid pBluescript was isolated from 1.5 ml Escherichia coli JM109 cell culture, following alkaline lysis yielding 8.2 micrograms high-quality DNA. Under similar binding conditions 21 micrograms of salmon sperm DNA bound to the ion exchangers. The affinity medium oligo-dT Magarose was demonstrated to bind 75 mumol of an oligo-dA probe/g of medium by hybridization. Under similar conditions mRNA could be isolated from a preparation of baby hamster cell total RNA. The magnetic susceptibility of Magarose is very high, facilitating the use of this separation technique for rapid batch chromatographic processes.

Animals↗
PubMed1992

Economic considerations important in the scale-up of an ovalbumin separation from hen egg-white on the anion-exchange cellulose DE92.

The scale-up of the separation of hen egg-white proteins has been investigated using Whatman DE92 anion-exchange cellulose. Having developed suitable chromatographic conditions, a maximum binding capacity of 100 mg protein/ml packed DE92 was determined in a 25-ml column. The process was scaled up 1000-fold and the influence of batch and column techniques on the chromatographic step assessed. Data indicate column processes to be more efficient than batch in the adsorptive stage.

Animals↗
PubMed1990

A simplified process for large-scale isolation of IgG from goat serum.

Immunoglobin G (IgG) is routinely used in many immunoassay systems. Whilst various laboratory-scale procedures exist for the isolation of IgG from host serum few are appropriate for scale-up. We have previously reported the improvement of an existing process for isolation of IgG from goat serum at laboratory scale (Schwartz et al., 1986) and in this study we took those improvements to pilot-scale and significantly reduced the process time and associated costs. Media fouling was reduced and product yield enhanced by utilisation of a guard column of the appropriate geometry. Isolation of pure IgG by anion-exchange chromatography was improved by selection of a suitable mobile phase and column loading parameters. Using a 10 1 column of QA52, 36 g of immunoelectrophoretically pure IgG was isolated from 7.2 1 of goat serum at an overall yield of 58%. Product recovery and purity were reproducible at pilot-scale under these conditions. A procedure for media clean-in-place (CIP) is described which also effects sterilisation and depyrogenation of the column and media.

Animals↗
PubMed1990

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.

Animals↗
PubMed1986

Purification and partial characterization of cat colon and submandibular gland kallikreins.

Kallikreins from cat colon and submandibular gland have been purified by acetone fractionation of tissue extracts, DEAE-Sephacel ion-exchange chromatography, rho-aminobenzamidine Sepharose 4B affinity chromatography and gel filtration on Sephadex G-75. They were of similar M.W., approximately 40,000, and each comprised five forms by isoelectric-focusing (pI 4.1-4.8). Both enzymes were potent kininogenases and exhibited similar specificities with synthetic ester and amide substrates. They were susceptible to a range of protease inhibitors. Surprisingly, neither was sensitive to aprotinin yet both were partially inhibited by soya-bean trypsin inhibitor. They were indistinguishable in our immunological tests. An acidic esterase (pI 2.2-3.5) of M.W. 120,000 was isolated from cat stomach by the same procedure. While it exhibited weak immunologic similarity to cat submandibular gland kallikrein, it had negligible kininogenase activity and different substrate and inhibitor specificities to the two kallikreins. It is concluded that similar tissue kallikreins are present in the colon and submandibular gland of the cat but are distinct from this cat stomach esterase.

Animals↗
PubMed1986

Purification and partial characterization of cat pancreatic and urinary kallikreins--comparison with other cat tissue kallikreins and related proteases.

Kallikreins have been purified from cat pancreas and urine by methods similar to those described previously for cat colon and submandibular gland kallikreins. The pancreatic kallikrein (M.W. 41,200, pI 4.75) was similar to the urinary kallikrein (M.W. 34,300 pI 4.35-4.70) in pH optimum, substrate specificity and inhibition profile. Both enzymes were potent kininogenases and immunologically similar. These enzymes closely resembled the kallikreins from cat colon and submandibular glands. A trypsin (M.W. 18,800) was isolated from cat pancreas and shown to be distinct from the group of kallikreins in all parameters tested. We attempted purification of cat renal kallikrein, but were unable to isolate any such enzyme. The major acidic esterase of cat kidney cortex (M.W. 59,000, pI 4.91) was purified and was distinct from both the cat tissue kallikreins and trypsin. The origin of cat urinary kallikrein remains unclear, but in the light of our findings, it may result from renal filtration of blood-borne tissue kallikreins rather than from intrarenal synthesis.

Animals↗
PubMed1982

A comparison of the catalytic activities of human plasma kallikreins I and II.

Subsites in the S2-S4 region [Schechter & Berger (1967) Biochem. Biophys. Res. Commun. 27, 157-162] were identified in human plasma kallikrein II (EC 3.4.21.8). Kinetic constants (kcat, Km) were determined for a series of seven extended N-aminoacyl-L-arginine methyl esters based on the C-terminal sequence of bradykinin (-Pro-Phe-Arg) or (Gly)n-Arg. With these substrates it was found that deacylation of the enzyme was rate-limiting. It was possible to infer that L-proline at residue P3 interacted with subsite S3 of the enzyme and L-phenylalanine at residue P2 interacts hydrophobically with subsite S2 in addition to hydrogen-bonded interactions with this subsite region. By comparison with the results of a similar study with human plasma kallikrein I, it is observed that although broadly similar subsite interactions occur between the two enzyme forms, the rate of deacylation of kallikrein II is approx. 35% of that observed for kallikrein I, and the latter form is up to ten times more active (in terms of kcat./Km) than kallikrein II.

Binding Sites↗
PubMed1982

Studies on the temperature-dependent autoinhibition of human plasma kallikrein I.

At 37 degrees C, human plasma kallikrein I follows Michaelis-Menten behaviour and exhibits a normal linear relationship between the initial velocity of hydrolysis of Ac-Pro-Phe-Arg-OMe,HCl and enzyme concentration in the range 0--150 pM. At temperatures of 30 degrees C and below substantial deviations from linearity are observed over the same enzyme concentration range. The temperature-dependent autoinhibition of kallikrein I activity is reversible and is not due to low-molecular-weight endogenous inhibitors or cofactors. The kinetic effect is apparently due to aggregation and can be abolished by the addition of sodium deoxycholate.

Binding Sites↗
PubMed1982

The kinetics of hydrolysis of some extended N-aminoacyl-L-arginine methyl esters by human plasma kallikrein. Evidence for subsites S2 and S3.

Subsites in the S2-S4 region were identified in human plasma kallikrein. Kinetic constants (kcat., Km) were determined for a series of seven extended N-aminoacyl-L-arginine methyl esters based on the C-terminal sequence of bradykinin (-Pro-Phe-Arg) or (Gly)n-Arg. The rate-limiting step for the enzyme-catalysed reaction was found to be deacylation of the enzyme. It was possible to infer that hydrogen-bonded interactions occur between substrate and the S2-S4 region of kallikrein. Insertion of L-phenylalanine at residue P2 demonstrates that there is also a hydrophobic interaction with subsite S2, which stabilizes the enzyme-substrate complex. The strong interaction demonstrated between L-proline at residue P3 and subsite S3 is of greatest importance in the selectivity of human plasma kallikrein. The purification of kallikrein from Cohn fraction IV of human plasma is described making use of endogenous Factor XIIf to activate the prekallikrein. Kallikreins I (Mr 91 000) and II (Mr 85 000) were purified 170- and 110-fold respectively. Kallikrein I was used for the kinetic work.

Arginine↗
PubMed1982

The kinetics of hydrolysis of some extended N-aminoacyl-L-arginine methyl esters by porcine pancreatic kallikrein. A comparison with human plasma Kallikrein.

The effects of subsite interactions in the S2-S4 region [Schechter & Berger (1967) Biochem. Biophys. Res. Commun. 27, 157-162] of porcine pancreatic kallikrein (EC 3.4.21.8) on its catalytic efficiency have been investigated. Kinetic constants (Kcat, Km) have been determined for a series of seven extended N-aminoacyl-L-arginine methyl esters whose sequence is based on either the C-terminal sequence of kallidin (-Pro-Phe-Arg) or (-Gly-)nArg. With these substrates it has been found that neither acylation nor deacylation of the enzyme is rate-limiting. Values of Kcat. range from 21.5 to 2320s-1, indicating that there are interactions with different residues in the N-aminoacyl chain and enzyme subsites in the S2-S4 region. It is shown that possible hydrogen-bonded interactions with the enzyme in the S3-S4 region have a significant effect on catalysis. The presence of L-phenylalanine at P2 has a very large effect on both Kcat, and Km, giving a greatly enhanced catalytic efficiency. Substrates with L-proline at P3 also have a marked effect, but in this case the overall effect is one of lowered catalytic efficiency. By comparison with the results of a similar study with human plasma kallikrein I (EC 3.4.21.8), it has been possible to demonstrate that there are considerable differences in kinetic behaviour between the two enzymes. These are related to relative differences in the rates of acylation and deacylation with ester substrates and also the roles of subsites S2 and S3 of the two enzymes.

Animals↗
PubMed1982

A possible relationship between human plasma kallikreins I and II.

Human plasma kallikrein I (EC 3.4.21.8; Mr 93 000) was found to undergo autolytic cleavage to form a protein resembling kallikrein II (Mr 85 000) plus a small peptide moiety. Conversion was found to be complete upon storage of kallikrein I solution at 4 degrees C for 7 days.

Dialysis↗