{"title":"固体颗粒在流态化过程中的运动","authors":"A. Bascoul, J.P. Couderc, H. Delmas","doi":"10.1016/0300-9467(93)80024-I","DOIUrl":null,"url":null,"abstract":"<div><p>Solid motion in liquid fluidized beds has been analysed using a radioactive particle and two detection devices partly superimposed, dividing the be</p><p>Particle velocity was determined by two different estimations, using the net flux across a zone frontier and the residence time between two successive</p><p>Particle dispersion coefficients, determined from residence time distribution, were also strongly increasing with increasing liquid velocity. It was co</p></div>","PeriodicalId":101225,"journal":{"name":"The Chemical Engineering Journal","volume":"51 3","pages":"Pages 135-150"},"PeriodicalIF":0.0000,"publicationDate":"1993-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0300-9467(93)80024-I","citationCount":"12","resultStr":"{\"title\":\"Mouvement des particules solides en fluidisation liquide solide\",\"authors\":\"A. Bascoul, J.P. Couderc, H. Delmas\",\"doi\":\"10.1016/0300-9467(93)80024-I\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Solid motion in liquid fluidized beds has been analysed using a radioactive particle and two detection devices partly superimposed, dividing the be</p><p>Particle velocity was determined by two different estimations, using the net flux across a zone frontier and the residence time between two successive</p><p>Particle dispersion coefficients, determined from residence time distribution, were also strongly increasing with increasing liquid velocity. It was co</p></div>\",\"PeriodicalId\":101225,\"journal\":{\"name\":\"The Chemical Engineering Journal\",\"volume\":\"51 3\",\"pages\":\"Pages 135-150\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1993-06-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/0300-9467(93)80024-I\",\"citationCount\":\"12\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"The Chemical Engineering Journal\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/030094679380024I\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"The Chemical Engineering Journal","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/030094679380024I","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Mouvement des particules solides en fluidisation liquide solide
Solid motion in liquid fluidized beds has been analysed using a radioactive particle and two detection devices partly superimposed, dividing the be
Particle velocity was determined by two different estimations, using the net flux across a zone frontier and the residence time between two successive
Particle dispersion coefficients, determined from residence time distribution, were also strongly increasing with increasing liquid velocity. It was co
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