The present paper describes an anion-exchange chromatography method to separate iron-free apo-Tf (apo-transferrin) from albumin and IgG in Cohn supernatant I. The method uses DEAE-fast flow Sepharose chromatography along with optimized protein concentration (5%, w/v) and column operation conditions (40 g/l, conductivity <1.0 mS/cm) to resolve apo-Tf from IgG and albumin. The single step purifies apo-Tf to >90% and provides an efficient means to obtain commercial quantities of the protein.
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http://dx.doi.org/10.1042/BA20050065 | DOI Listing |
J Chromatogr A
August 2020
State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China. Electronic address:
Plasma fractionation industry is by far the largest protein pharmaceutical provider, but there are still some plasma components in its industrial waste liquid that have not been utilized. This study aimed to develop a simple and efficient method for plasma protein recovery from Cohn fraction V supernatant (FVS), an effluent containing about 40% ethanol. A new affinity chromatography medium was synthesized with a fatty acid ligand.
View Article and Find Full Text PDFMicroorganisms
May 2020
Microbial Processes and Interactions (MiPI), TERRA Research Center, Gembloux Agro-Bio Tech, University of Liege, 5030 Gembloux, Belgium.
Two fungi, i.e., Link and (Ahlb.
View Article and Find Full Text PDFTransfusion
April 2018
Department of Laboratory Medicine and Pathology, University of Minnesota, Minneapolis, Minnesota.
Background: Platelets (PLTs) collected and stored in PLT additive solution Intersol (PAS-C) are presumed to reduce recipient exposure to donor plasma components; however, the effects of PAS-C on PLT supernatant composition are poorly defined. Therefore, we compared the total protein concentration, isohemagglutinin titers, and HLA antibodies in supernatants of PAS-C PLTs to plasma PLTs.
Study Design And Methods: Apheresis PLTs from group O blood donors were collected into either 100% donor plasma (n = 50) or a mixture of 65% PAS-C/35% donor plasma (n = 50).
Biotechnol Bioeng
July 2015
Karlsruhe Institute of Technology, Engler-Bunte-Ring 1, 76131, Karlsruhe, Germany.
Pooling decisions in preparative liquid chromatography for protein purification are usually based on univariate UV absorption measurements that are not able to differentiate between product and co-eluting contaminants. This can result in inconsistent pool purities or yields, if there is a batch-to-batch variability of the feedstock. To overcome this analytical bottleneck, a tool for selective inline quantification of co-eluting model proteins using mid-UV absorption spectra and Partial Least Squares Regression (PLS) was presented in a previous study and applied for real-time pooling decisions.
View Article and Find Full Text PDFJ Chromatogr B Analyt Technol Biomed Life Sci
October 2014
Research and Development Department, CSL Behring (Australia), 189-209 Camp Rd, Broadmeadows, Victoria 3047, Australia.
The manufacture of human serum albumin by chromatographic procedures involves gel filtration chromatography as a final polishing step. Despite this step being essential to remove high molecular weight impurity proteins and thus ensure a stable and safe final product, it is relatively inefficient. This paper explores the use of hydrophobic charge induction chromatographic media, MEP HyperCel as an alternative to Sephacryl S200HR gel filtration for the polishing of human serum albumin derived by ion exchange chromatographic purification of Cohn Supernatant I.
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