{"title":"Rapid characterization of flow regimes in multiphase reactors through box-counting dimensions with an embedding dimension of two","authors":"C.L. Briens, C. Hudson, L.A. Briens","doi":"10.1016/S0923-0467(96)03129-6","DOIUrl":null,"url":null,"abstract":"<div><p>The performance of multiphase reactors is greatly affected by their flow regime. The box-counting dimension of a probe signal characterizes its intrinsic, dimensionless structure and is not significantly affected by moderate changes in probe calibration constants. Using the box-counting dimension to characterize the flow regime can, thus, eliminate problems associated with changes in probe, liquid or solid characteristics. This study uses an approximate box-counting dimension which is so rapidly calculated that it could be used for on-line control. The box-counting dimension of the raw signal from a bubble probe allows the accurate detection of gas maldistribution in bubble columns and gas-liquid-solid fluidized beds. The box-counting dimension of the raw signal from a local conductivity probe allows the accurate detection of liquid maldistribution in bubble columns and gas-liquid-solid fluidized beds. The fluidization regime of liquid-solid and gas-liquid-solid beds can be accurately identified from the box-counting dimension of the signal recorded with either local probes or cross-sectional probes. The complete fluidization of a liquid-solid bed of splinter-like particles can be determined from the box-counting dimension of the signals from either a local probe or trace rinjection experiments.</p></div>","PeriodicalId":101226,"journal":{"name":"The Chemical Engineering Journal and the Biochemical Engineering Journal","volume":"64 1","pages":"Pages 169-178"},"PeriodicalIF":0.0000,"publicationDate":"1996-10-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/S0923-0467(96)03129-6","citationCount":"3","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"The Chemical Engineering Journal and the Biochemical Engineering Journal","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0923046796031296","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 3
Abstract
The performance of multiphase reactors is greatly affected by their flow regime. The box-counting dimension of a probe signal characterizes its intrinsic, dimensionless structure and is not significantly affected by moderate changes in probe calibration constants. Using the box-counting dimension to characterize the flow regime can, thus, eliminate problems associated with changes in probe, liquid or solid characteristics. This study uses an approximate box-counting dimension which is so rapidly calculated that it could be used for on-line control. The box-counting dimension of the raw signal from a bubble probe allows the accurate detection of gas maldistribution in bubble columns and gas-liquid-solid fluidized beds. The box-counting dimension of the raw signal from a local conductivity probe allows the accurate detection of liquid maldistribution in bubble columns and gas-liquid-solid fluidized beds. The fluidization regime of liquid-solid and gas-liquid-solid beds can be accurately identified from the box-counting dimension of the signal recorded with either local probes or cross-sectional probes. The complete fluidization of a liquid-solid bed of splinter-like particles can be determined from the box-counting dimension of the signals from either a local probe or trace rinjection experiments.