Grafting reactions and heparin adsorption of poly(amidoamine)-grafted poly(urethane amide)s.

Differently terminated poly(amidoamine) (PAA) oligomers were grafted on the surface of poly(ether urethane amide)s (PEUAm), with fumaric or maleic acid moieties. The grafting reaction was Michael-type addition of amino groups to activated double bonds in the PEUAm backbone. PAAs having primary amino, or secondary amino end-groups were directly grafted on the surface of PEUAm sheets. For vinyl-terminated chains an alpha, omega amino-polyether spacer was introduced initially, following the same addition mechanism. Ungrafted and grafted materials were characterized, besides other analytical techniques, by ATR FT-IR spectroscopy. The heparin adsorption on PEAUm films was analysed after its elution from heparinized samples, quantified by coagulation tests (aPTT), and related to the presence of the PAAs chains grafted on to the surface. Results indicate that PAA-grafted PEUAm elastomeric biomaterials, display enhanced heparin adsorption abilities.

Charge heterogeneity of recombinant pro-urokinase and urinary urokinase, as revealed by isoelectric focusing in immobilized pH gradients.

When analysing homogeneous preparations of recombinant pro-urokinase and urinary urokinase by isoelectric focusing (IEF) in immobilized pH gradients, an extreme charge heterogeneity was detected (at least ten major and ten minor bands in the pH range 7-10). This extensive polydispersity was not caused by different degrees of glycosylation, or by IEF artefacts, such as binding to carrier ampholytes or carbamylation by urea. A great part of this heterogeneity could be traced back to the existence of a multitude of protein molecules containing Cys residues at different oxidation levels (-SH, -S-S-, even cysteic acid). Owing to the very large number of Cys residues in pro-urokinase (24 out of a total of 411 amino acids) and to the relatively high pI of its native forms (pI 9.5-9.8; the native form is believed to contain all Cys residues as -S-S- bridges), the presence of SH or cysteic acid residues would increase the negative surface charge, as even SH groups would be extensively ionized. In pro-urokinase, part of the heterogeneity was also due to spontaneous degradation to urokinase and possibly also to cleavage into lower-molecular-mass fragments. When all these causes of heterogeneity were removed, the pI spectrum was reduced to only four, about equally intense bands. The cause of this residual heterogeneity is unknown.

Use of polybuffer as carrier ampholytes in mixed-bed Immobiline gels for isoelectric focusing.

In mixed-bed, carrier ampholyte-Immobiline gels, a primary, insolubilized pH gradient is admixed with a secondary, soluble pH gradient generated by amphoteric buffers. The latter are the standard carrier ampholytes (e.g. Ampholine, Pharmalyte, Biolyte, Servalyte), used in conventional isoelectric focusing, admixed to Immobiline gels in levels of approximately 0.5-1%. It is here shown that polybuffers 96 (covering the pH 6-9 range) and 74 (covering the pH 4-7 interval) used as eluents in chromatofocusing, can effectively substitute the standard carrier ampholytes with considerable savings (they are 1/16th as expensive as the latter chemicals).

Isoelectric protein purification by orthogonally coupled hydraulic and electric transports in a segmented immobilized pH gradient.

A new method is described for preparative protein purification, based on isoelectric focusing on immobilized pH gradients. The principle is entirely new, as it is based on keeping the protein of interest isoelectric, in a flow-chamber, and focusing the impurities in the Immobiline gel. For this, a hydraulic flow is coupled orthogonally to an electric flow, sweeping away the non-isoelectric impurities from the recycling chamber. The sample flow-chamber is built in the centre of the apparatus, and is coupled to an upper and lower segment of an immobilized pH gradient. The protein to be purified is kept isoelectric in the flow-chamber and prevented from leaving it by arranging for the extremities of the immobilized pH gradient, forming the ceiling and the floor of this chamber, to have isoelectric points just higher (e.g. +0.05 pH units, on the cathodic side) and just lower (e.g. -0.05 pH units, on the anodic side) than the known pI of the species of interest. Macromolecules and small ions leave the flow chamber at a rate corresponding to a first order reaction kinetics (the plot of log C vs. time being linear). In general, for macromolecules, 12 h of recycling under current allow removal of 95% impurities. After 24 h of recycling, the protein of interest is more than 99.5% pure. The recoveries are very high (approaching 100%) as the sample under purification never enters the Immobiline gel and thus does not have to be extracted from a hydrophilic matrix, as typical of preparative gel electrophoresis.

Protein desalting by isoelectric focusing in a segmented immobilized pH gradient.

We have recently described an apparatus for protein purification based on a segmented Immobiline gel, having one or more liquid interlayers in between. The principle is entirely new, as it is based on keeping the protein of interest isoelectric, in a flow chamber, and focusing the impurities in an Immobiline gel. For this, a hydraulic flow is coupled orthogonally to an electric flow, sweeping away the non-isoelectric impurities from the recycling chamber. We now demonstrate that the present apparatus can be efficiently used for protein desalting. Hemoglobin A samples, containing 50 mM NaCl or 50 mM ammonium acetate, could be efficiently desalted in 2 h of recycling, after which the total salt content had decreased to less than 0.005 mM (a salt decrement of more than 10,000 fold the initial input). However, with polyprotic buffers (sulphate, citrate, phosphate, oligoamines) the desalting process was much slower, typically of the order of 20 h, possibly due to interaction of these species with the surrounding Immobiline matrix. In this last case, outside pH control (e.g. with a pH-stat) is necessary during protein purification, as, due to the faster removal of the monovalent counterion, the solution in the recycling chamber can become rather acidic or alkaline. It is demonstrated that the 2 extremities of the Immobiline segments facing the sample recycling chamber act indeed as isoelectric membranes, having a good buffering capacity, preventing the protein macroion from leaving the chamber by continuously titrating it to its isoelectric point.

Isoelectric protein purification in segmented immobilized pH gradients. Effect of salts on rate of contaminants' removal.

A method is described for keeping a constant salt background during protein purification in a segmented immobilized pH gradient. It is based on an external hydraulic flow replenishing the salt loss due to combined electric and diffusional mass transport (similar to the concept of Ribes' steady-state rheoelectrolysis). Such a minimum of ionic strength might be needed for proteins which tend to precipitate and aggregate at or in vicinity of the isoelectric point. However, it is found that any salt level in the sample feed (already at 1 mM concentration) deteriorates transport of non-isoelectric proteins, because of the much larger current fraction carried by the ions themselves as opposed to proteins. In addition, high salt levels in the sample reservoir might form cathodic and anodic ion boundaries, alkaline and acidic, respectively, which might hamper protein migration and even induce denaturation. Thus, when high salt backgrounds are needed in the sample feed, external pH control should be exerted, e.g. with a pH-stat. Three parameters influence protein transport in the segmented IPG chamber: (a) cross-sectional area of the Immobiline membranes; (b) delta pI between the isoelectric protein and the contaminants and (c) salt molarity in the sample reservoir. The first 2 show a positive, the last a negative correlation.

A horizontal apparatus for isoelectric protein purification in a segmented immobilized pH gradient.

A modification of the previously described apparatus (Faupel et al. (1987) J. Biochem. Biophys. Methods 15, 147-162), for recycling isoelectric focusing in a segmented immobilized pH gradient, is here reported. The most important improvements are: (1) a horizontal, vs. the previously vertical assembly; (2) a reduction of the thickness of the central flow chamber to 6 mm, vs. the previous 3 cm length and (3) the introduction, at both gel extremities of each Immobiline segment, of polypropylene filters, thus efficiently blocking the gel in situ. The advantages are: (i) the spontaneous removal of air bubbles, which in the vertical apparatus tend to accumulate in the ceiling of the flow chamber and to obstruct the flow of electric current; (ii) a more efficient hydraulic flow with a reduced chance of heating the liquid stream in the flow chamber, due to its reduced length along the separation path and (iii) a reduced risk of gel detachment from the tube walls, due to osmotic swelling caused by focused protein zones in the gel phase and by the fixed Immobiline charges in the polyacrylamide matrix.