Abstract: Matrices for electrokinetic and chromatographic separations, based on a unique class of mono- and disubstituted (on the amido nitrogen) acrylamides (e.g., acrylamido-N-ethoxy ethanol, acrylamido-N,N-diethoxy ethanol) off erthe following advantages: a) strong resistance to the alkaline hydrolysis (most zone separations occurring at basic pH values); b) a high hydrophilicity; and c) greater porosity, due to the larger M.sub.r value of the monomers. Such matrices can be prepared as `chemically crosslinked` gels or as `physical` gels, the latter consisting of strings of monofunctional monomer in the absence of crosslinker, at concentrations above the entanglement threshold. It is moreover possible to further increment the gel porosity by polymerizing it in the presence of laterally aggregating agents (e.g., polyethylene glycol of M.sub.r 6-20,000 Da), thus obtaining matrices which allow better resolution of large M.sub.

Abstract: Described is an isoelectric focusing electrophoretic process for the separation and purification of an amphoteric or neutral chemical compound from one or more electrically charged chemical compound(s). Said process is illustrated below at the example of the purification of a protein from contaminating proteins and salts. It may be carried out in an apparatus especially designed therefor, e.g. an apparatus as depicted in FIG. 1. Said apparatus and various modifications thereof are also claimed. The mixture to be separated is present within a hydraulic flow in chamber 8. Cylinders 5 and 12 contain immobilized pH-gradients or are replaced by amphoteric isoelectric pH-membranes. Each of said pH-gradients and pH-membranes has conductivity and both buffering and titrant capacity in its pH-interval.

Abstract: Described is an isoelectric focusing electrophoretic process for the separation and purification of an amphoteric or neutral chemical compound from one or more electrically charged chemical compound(s). Said process is illustrated below at the example of the purification of a protein from contaminating proteins and salts. It may be carried out in an apparatus especially designed therefor, e.g. an apparatus as depicted in FIG. 1. Said apparatus and various modifications thereof are also claimed. The mixture to be separated is present within a hydraulic flow in chamber 8. Cylinders 5 and 12 contain immobilized pH-gradients or are replaced by amphoteric isoelectric pH-membranes. Each of said pH-gradients and pH-membranes has conductivity and both buffering and titrant capacity in its pH-interval.