{"title":"蛋白A亲和层析法纯化人IgG3的规模化研究。","authors":"J Amaral, M Inganäs, J Cabral, D Prazeres","doi":"10.1023/a:1016353419499","DOIUrl":null,"url":null,"abstract":"<p><p>The purification of human IgG3 subclass out of IgG (Immunoglobulin-G) was studied using protein A-Sepharose affinity chromatography. The effect of operational parameters such as flow rate, ionic strength, pH and size of sample was investigated, and the process was scaled-up 10-fold. The use of 0.5 m NaCl in the loading buffer had a dramatic effect in the purity of IgG3 recovered in the flowthrough fraction (values in the order of 97% were consistently obtained). This was attributed to a more effective binding of IgG subclasses 1, 2 and 4 to protein A (well known classical mechanism based in Fc fragment) and in some extent to a decrease in the binding of subclass 3 to protein A by the alternative mechanism based in the Fab fragment. The increase in residence time also increased in a relevant way the purity of IgG3. This is attributed to an increased effectiveness of the mechanisms mentioned above. The recovery yields in the IgG3 rich fraction were in the range 21-32% and are possibly a consequence of binding to protein A by the alternative mechanism and also due to deactivation during processing.</p>","PeriodicalId":9179,"journal":{"name":"Bioseparation","volume":"10 4-5","pages":"139-43"},"PeriodicalIF":0.0000,"publicationDate":"2001-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1023/a:1016353419499","citationCount":"4","resultStr":"{\"title\":\"Study on the scale-up of human IgG3 purification using protein A affinity chromatography.\",\"authors\":\"J Amaral, M Inganäs, J Cabral, D Prazeres\",\"doi\":\"10.1023/a:1016353419499\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p><p>The purification of human IgG3 subclass out of IgG (Immunoglobulin-G) was studied using protein A-Sepharose affinity chromatography. The effect of operational parameters such as flow rate, ionic strength, pH and size of sample was investigated, and the process was scaled-up 10-fold. The use of 0.5 m NaCl in the loading buffer had a dramatic effect in the purity of IgG3 recovered in the flowthrough fraction (values in the order of 97% were consistently obtained). This was attributed to a more effective binding of IgG subclasses 1, 2 and 4 to protein A (well known classical mechanism based in Fc fragment) and in some extent to a decrease in the binding of subclass 3 to protein A by the alternative mechanism based in the Fab fragment. The increase in residence time also increased in a relevant way the purity of IgG3. This is attributed to an increased effectiveness of the mechanisms mentioned above. The recovery yields in the IgG3 rich fraction were in the range 21-32% and are possibly a consequence of binding to protein A by the alternative mechanism and also due to deactivation during processing.</p>\",\"PeriodicalId\":9179,\"journal\":{\"name\":\"Bioseparation\",\"volume\":\"10 4-5\",\"pages\":\"139-43\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2001-01-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1023/a:1016353419499\",\"citationCount\":\"4\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Bioseparation\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.1023/a:1016353419499\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Bioseparation","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1023/a:1016353419499","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 4
摘要
采用蛋白A-Sepharose亲和层析法从IgG(免疫球蛋白- g)中纯化人IgG3亚类。考察了流速、离子强度、pH、样品粒度等操作参数对该工艺的影响,并将工艺放大了10倍。在上样缓冲液中使用0.5 m NaCl,对流动馏分中回收的IgG3纯度有显著影响(一致达到97%左右)。这是由于IgG亚类1、2和4与蛋白a的结合更有效(众所周知的基于Fc片段的经典机制),在某种程度上,基于Fab片段的替代机制减少了IgG亚类3与蛋白a的结合。停留时间的增加也相应提高了IgG3的纯度。这是由于上述机制的有效性有所提高。富含IgG3的部分的回收率在21-32%之间,这可能是通过替代机制与蛋白a结合的结果,也可能是由于加工过程中的失活。
Study on the scale-up of human IgG3 purification using protein A affinity chromatography.
The purification of human IgG3 subclass out of IgG (Immunoglobulin-G) was studied using protein A-Sepharose affinity chromatography. The effect of operational parameters such as flow rate, ionic strength, pH and size of sample was investigated, and the process was scaled-up 10-fold. The use of 0.5 m NaCl in the loading buffer had a dramatic effect in the purity of IgG3 recovered in the flowthrough fraction (values in the order of 97% were consistently obtained). This was attributed to a more effective binding of IgG subclasses 1, 2 and 4 to protein A (well known classical mechanism based in Fc fragment) and in some extent to a decrease in the binding of subclass 3 to protein A by the alternative mechanism based in the Fab fragment. The increase in residence time also increased in a relevant way the purity of IgG3. This is attributed to an increased effectiveness of the mechanisms mentioned above. The recovery yields in the IgG3 rich fraction were in the range 21-32% and are possibly a consequence of binding to protein A by the alternative mechanism and also due to deactivation during processing.