Claudio Fabiani , Luigi Bimbi , Massimo Pizzichini , Luigi Santarossa
{"title":"中空纤维膜装置在富氧空气生产中的性能","authors":"Claudio Fabiani , Luigi Bimbi , Massimo Pizzichini , Luigi Santarossa","doi":"10.1016/0950-4214(96)00012-6","DOIUrl":null,"url":null,"abstract":"<div><p>The performance of a pilot test for biogas upgrading has been tested under different process conditions to produce oxygen-enriched air for aqueous media application. The selectivity of the polysulfone hollow fibres for <span><math><mtext>N</mtext><msub><mi></mi><mn>2</mn></msub><mtext>O</mtext><msub><mi></mi><mn>2</mn></msub></math></span> permeation allows the production of an oxygen-enriched air stream in the 30–50% range and an inert gas (nitrogen between 82–98%) by operating the pilot unit at different stage-cut values in a single pass mode. Membrane area requirements for a medium size plant of 100 Nm<sup>3</sup> h<sup>−1</sup> are discussed according to a simple perfect mixing model for gas permeation.</p></div>","PeriodicalId":12586,"journal":{"name":"Gas Separation & Purification","volume":"10 1","pages":"Pages 75-79"},"PeriodicalIF":0.0000,"publicationDate":"1996-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0950-4214(96)00012-6","citationCount":"8","resultStr":"{\"title\":\"Performance of a hollow fibre membrane unit in oxygen-enriched air production\",\"authors\":\"Claudio Fabiani , Luigi Bimbi , Massimo Pizzichini , Luigi Santarossa\",\"doi\":\"10.1016/0950-4214(96)00012-6\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>The performance of a pilot test for biogas upgrading has been tested under different process conditions to produce oxygen-enriched air for aqueous media application. The selectivity of the polysulfone hollow fibres for <span><math><mtext>N</mtext><msub><mi></mi><mn>2</mn></msub><mtext>O</mtext><msub><mi></mi><mn>2</mn></msub></math></span> permeation allows the production of an oxygen-enriched air stream in the 30–50% range and an inert gas (nitrogen between 82–98%) by operating the pilot unit at different stage-cut values in a single pass mode. Membrane area requirements for a medium size plant of 100 Nm<sup>3</sup> h<sup>−1</sup> are discussed according to a simple perfect mixing model for gas permeation.</p></div>\",\"PeriodicalId\":12586,\"journal\":{\"name\":\"Gas Separation & Purification\",\"volume\":\"10 1\",\"pages\":\"Pages 75-79\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1996-01-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/0950-4214(96)00012-6\",\"citationCount\":\"8\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Gas Separation & Purification\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/0950421496000126\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Gas Separation & Purification","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/0950421496000126","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Performance of a hollow fibre membrane unit in oxygen-enriched air production
The performance of a pilot test for biogas upgrading has been tested under different process conditions to produce oxygen-enriched air for aqueous media application. The selectivity of the polysulfone hollow fibres for permeation allows the production of an oxygen-enriched air stream in the 30–50% range and an inert gas (nitrogen between 82–98%) by operating the pilot unit at different stage-cut values in a single pass mode. Membrane area requirements for a medium size plant of 100 Nm3 h−1 are discussed according to a simple perfect mixing model for gas permeation.