CAS OpenIR
Hydrodynamics and mass transfer in a slurry external airlift loop reactor integrating mixing and separation
Geng, Shujun1,3,6; Li, Zhuo1,2; Liu, Hongyan2; Yang, Chao1,4; Gao, Fei5; He, Taobo5; Huang, Qingshan1,3,4,6
2020-01-16
Source PublicationCHEMICAL ENGINEERING SCIENCE
ISSN0009-2509
Volume211Pages:10
AbstractA pilot external airlift loop reactor (EALR) integrating mixing and separation was first proposed by combining directional flow in the EALR and liquid-solid separation in two parallel hydrocyclones. In this developed reactor, mixing, mass transfer, and liquid-solid separation can be simultaneously realized without extra energy input. Technical feasibility was firstly verified, and then hydrodynamics and mass transfer were measured. It was found that the minimum diameter of solid particles retained for circulation was 6.82 mu m, and the treatment capacity of clean liquid was up to 3.0 m(3)/h. Additionally, global gas holdup, liquid circulating velocity, and volumetric mass transfer coefficient increased monotonously with increasing the superficial gas velocity while declined with the increase of solid concentration. Axial inhomogeneity of solid particles was decayed with increasing the superficial gas velocity and solid concentration. This new type of slurry EALR is promising to be applied in the gas-liquid-solid catalytic industries. (C) 2019 Elsevier Ltd. All rights reserved.
KeywordExternal airlift loop reactor Mixing Separation Hydrocyclone Hydrodynamics Mass transfer
DOI10.1016/j.ces.2019.115294
Language英语
WOS KeywordCIRCULATION LIQUID VELOCITY ; FLOW REGIME TRANSITION ; GAS HOLD-UP ; BUBBLE-COLUMN ; TRANSFER COEFFICIENT ; HEAT-TRANSFER ; BEHAVIOR ; SOLIDS ; WATER ; DISTRIBUTIONS
Funding ProjectNational Natural Science Foundation of China[21808234] ; National Natural Science Foundation of China[21878318] ; National Natural Science Foundation of China[91434114] ; Instrument Developing Project of the CAS[YZ201641] ; "Transformational Technologies for Clean Energy and Demonstration", Strategic Priority Research Program of the CAS[XDA21060400] ; QIBEBT of the CAS[QIBEBT ZZBS201803] ; Dalian National Laboratory for Clean Energy of the CAS[QIBEBT ZZBS201803] ; CAS Key Technology Talent Program ; Project of CNPC-DICP Joint Research Center
WOS Research AreaEngineering
WOS SubjectEngineering, Chemical
Funding OrganizationNational Natural Science Foundation of China ; Instrument Developing Project of the CAS ; "Transformational Technologies for Clean Energy and Demonstration", Strategic Priority Research Program of the CAS ; QIBEBT of the CAS ; Dalian National Laboratory for Clean Energy of the CAS ; CAS Key Technology Talent Program ; Project of CNPC-DICP Joint Research Center
WOS IDWOS:000498520300028
PublisherPERGAMON-ELSEVIER SCIENCE LTD
Citation statistics
Document Type期刊论文
Identifierhttp://ir.ipe.ac.cn/handle/122111/38374
Collection中国科学院过程工程研究所
Corresponding AuthorHuang, Qingshan
Affiliation1.Chinese Acad Sci, Qingdao Inst Bioenergy & Bioproc Technol QIBEBT, Key Lab Biofuels, Qingdao 266101, Shandong, Peoples R China
2.Hebei Univ Technol, Sch Chem Engn & Technol, Tianjin 300130, Peoples R China
3.Dalian Natl Lab Clean Energy DNL, Dalian 116023, Liaoning, Peoples R China
4.Chinese Acad Sci, Inst Proc Engn, Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
5.CNPC, Petrochem Res Inst, Beijing 100083, Peoples R China
6.Univ Chinese Acad Sci, Beijing 100080, Peoples R China
Recommended Citation
GB/T 7714
Geng, Shujun,Li, Zhuo,Liu, Hongyan,et al. Hydrodynamics and mass transfer in a slurry external airlift loop reactor integrating mixing and separation[J]. CHEMICAL ENGINEERING SCIENCE,2020,211:10.
APA Geng, Shujun.,Li, Zhuo.,Liu, Hongyan.,Yang, Chao.,Gao, Fei.,...&Huang, Qingshan.(2020).Hydrodynamics and mass transfer in a slurry external airlift loop reactor integrating mixing and separation.CHEMICAL ENGINEERING SCIENCE,211,10.
MLA Geng, Shujun,et al."Hydrodynamics and mass transfer in a slurry external airlift loop reactor integrating mixing and separation".CHEMICAL ENGINEERING SCIENCE 211(2020):10.
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