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Protein purification dialysis

Purify the sulfhydryl-modified protein by dialysis against 50mM sodium phosphate, 1 mM EDTA, pH 7.5, or by gel filtration on a Sephadex G-25 column using the same buffer. Again, if a peptide of low molecular weight is being modified, use careful gel filtration for purification. [Pg.75]

The classical approach to preliminary protein purification (including allergens) includes its desalting from previously prepared crude extracts using (NH4)2S04. This is followed by dialysis and subsequent purification. [Pg.87]

Artificial semipermeable membranes are routinely used in biochemical laboratories to separate small solutes from larger solutes. For example, this technique (referred to as dialysis) is used as an important early step in protein purification. An impure protein-containing specimen is placed in a cellophane dialysis bag (Figure 3B), which is then suspended in flowing distilled water or in a buffered solution. After a certain time, all the small solutes leave the bag. The protein solution, which may contain many high-molecular-weight impurities, is then ready for further purification. [Pg.91]

In contrast to enzymatic catalyst optimization, artificial metalloenzymes require purified protein samples in milligram quantities. These requirements severely slow down the screening process, the bottleneck being the protein purification by affinity chromatography, followed by dialysis and lyophilization. To accelerate this process, a straightforward extraction-immobilization protocol with biotin-sepharose was implemented to capture functional Sav from crude cellular extracts (Fig. 8) [39, 57], This procedure significantly hastened the optimization process, at the cost of a slight erosion in selectivity. [Pg.108]

Countless are the circumstances that cause a protein purification to fail the column draws air, the pump tube is worn through, the wrong buffer was used, inlet or outlet tubes are leaking, the column is blocked, the dialysis tube has a hole, the cooling cell fails, and fraction collectors have a tendency to quit just when the precious protein eludes in the last purification step. Lucky is he who owns a pump, has a reliable fraction collector (e.g., from Gilson) and good columns (e.g., from Pharmacia), and does not have to lend these tools to colleagues. [Pg.110]

The end point of many protein purifications is SDS gel electrophoresis. The protein to be sequenced thus occurs as a band in the gel. Hunkapiller et al. (1983) gently stain the band (e.g., with Na-acetate), cut out the gel piece, and elude the protein in a dialysis chamber. The eluate is applied to a filter and then sequenced. The method is reliable but complicated and has a low yield. Prussak et al. (1989) do without a dialysis chamber and elude the protein via passive diffusion in the presence of 0.01% SDS. [Pg.179]

Fig. 1 Schematic diagram From membrane protein purification over reconstitution into dialysis vesides to patch damp technique (adapted from ref. 5). Fig. 1 Schematic diagram From membrane protein purification over reconstitution into dialysis vesides to patch damp technique (adapted from ref. 5).
A major nonhemodialysis application of countercurrent dialysis (CCD) is the buffer exchange of proteins in the biopharmaceutical industry. In multistep biopharma-ceutical production processes, the buffer solution constituents often have to be exchanged for protein purification steps. The original buffer solution, for example, may contain, say, 0.5 M ammonium sulfate and 0.05 M sodium phosphate (plus protein and other constituents) the CCD... [Pg.761]

Water soluble protein with a relative molecular mass of ca. 32600, which particularly contains copper and zinc bound like chelate (ca. 4 gram atoms) and has superoxide-dismutase-activity. It is isolated from bovine liver or from hemolyzed, plasma free erythrocytes obtained from bovine blood. Purification by manyfold fractionated precipitation and solvolyse methods and definitive separation of the residual foreign proteins by denaturizing heating of the orgotein concentrate in buffer solution to ca. 65-70 C and gel filtration and/or dialysis. [Pg.1493]

The protein was purified by a dialysis procedure, denatured and analysed by sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE). Western blotting indicated that the protein of interest consisted of two components, one of which increased in concentration as the purification proceeded. The authors initially suggested that this could be due to the presence of a number of species produced by modification of the amino acid side-chains, for example, by glyco-sylation, or by modification of the C- or N- terminus. [Pg.198]

Purify the modified protein from reaction by-products by dialysis or gel filtration using 50 mM sodium phosphate, 0.15 M NaCl, 10 mM EDTA, pH 7.2. Alternatively, centrifugal spin columns containing a desalting resin may be used for rapid purification (Thermo Fisher). [Pg.280]

Liposomes containing PE lipid components may be activated with these crosslinkers to contain iodoacetyl derivatives on their surface (Figure 22.29). The reaction conditions described in Chapter 5, Section 1.5 may be used, substituting a liposome suspension for the initial protein being modified in that protocol. The derivatives are stable enough in aqueous solution to allow purification of the modified vesicles from excess reagent (by dialysis or gel filtration) without... [Pg.898]

Standard tests, dialysis, heat inactivation, and the effects of changing the pH on the catalytic activity of the preparations, were all consistent with the idea that enzymes had the properties ascribed to proteins. Between 1920 and 1930 increasing numbers of enzymes were isolated by Willstatter and partially purified. Assays for purification and the extent achieved were not sufficiently rigorous to exclude the possi-... [Pg.183]


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See also in sourсe #XX -- [ Pg.69 , Pg.69 ]




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