{"title":"非均匀法向速度多孔垂直壁上的层流冷凝","authors":"C.Y. Liu, K.A.R. Ismail, C.D. Ebinuma","doi":"10.1016/0094-4548(81)90059-X","DOIUrl":null,"url":null,"abstract":"<div><p>Similar solution has been obtained to the problem of laminar film condensation on a porous wall when the normal velocity at the wall is proportional to <span><math><mtext>-1</mtext><mtext>4</mtext></math></span> th the power of longitudinal coordinate. Both temperature and velocity profiles are calculated. The effect of normal velocity at the wall on the profiles as well as on the heat transfer can be observed.</p></div>","PeriodicalId":100875,"journal":{"name":"Letters in Heat and Mass Transfer","volume":"8 6","pages":"Pages 509-514"},"PeriodicalIF":0.0000,"publicationDate":"1981-11-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0094-4548(81)90059-X","citationCount":"0","resultStr":"{\"title\":\"Laminar film condensation on a porous vertical wall with non-uniform normal velocity\",\"authors\":\"C.Y. Liu, K.A.R. Ismail, C.D. Ebinuma\",\"doi\":\"10.1016/0094-4548(81)90059-X\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Similar solution has been obtained to the problem of laminar film condensation on a porous wall when the normal velocity at the wall is proportional to <span><math><mtext>-1</mtext><mtext>4</mtext></math></span> th the power of longitudinal coordinate. Both temperature and velocity profiles are calculated. The effect of normal velocity at the wall on the profiles as well as on the heat transfer can be observed.</p></div>\",\"PeriodicalId\":100875,\"journal\":{\"name\":\"Letters in Heat and Mass Transfer\",\"volume\":\"8 6\",\"pages\":\"Pages 509-514\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1981-11-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/0094-4548(81)90059-X\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Letters in Heat and Mass Transfer\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/009445488190059X\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Letters in Heat and Mass Transfer","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/009445488190059X","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Laminar film condensation on a porous vertical wall with non-uniform normal velocity
Similar solution has been obtained to the problem of laminar film condensation on a porous wall when the normal velocity at the wall is proportional to th the power of longitudinal coordinate. Both temperature and velocity profiles are calculated. The effect of normal velocity at the wall on the profiles as well as on the heat transfer can be observed.