Modeling the Mean Residence Time of Liquid Phase in the Gas–Liquid Cyclone
Residence time is a key parameter for the cyclones with mass transfer or reaction process. A model for the cylinder-on-cone cyclone was presented to calculate the mean residence time of the liquid phase, based on a force balance on the wall film. This model was validated using an experiment, which m...
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Published in | Industrial & engineering chemistry research Vol. 54; no. 43; pp. 10885 - 10892 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
American Chemical Society
04.11.2015
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Abstract | Residence time is a key parameter for the cyclones with mass transfer or reaction process. A model for the cylinder-on-cone cyclone was presented to calculate the mean residence time of the liquid phase, based on a force balance on the wall film. This model was validated using an experiment, which measured the residence time of the liquid phase by the hold-up method. The results demonstrated that the predicted residence times are in good overall agreement with the measured values. Furthermore, the liquid residence time decreases obviously with increasing droplets loading, and decreases less with increasing inlet velocity. The liquid residence time increases with the cylinder diameter. The wall film velocity, however, decreases with increasing cylinder diameter, because the perimeter of liquid wall film is directly proportional to the cylinder diameter. |
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AbstractList | Residence time is a key parameter for the cyclones with mass transfer or reaction process. A model for the cylinder-on-cone cyclone was presented to calculate the mean residence time of the liquid phase, based on a force balance on the wall film. This model was validated using an experiment, which measured the residence time of the liquid phase by the hold-up method. The results demonstrated that the predicted residence times are in good overall agreement with the measured values. Furthermore, the liquid residence time decreases obviously with increasing droplets loading, and decreases less with increasing inlet velocity. The liquid residence time increases with the cylinder diameter. The wall film velocity, however, decreases with increasing cylinder diameter, because the perimeter of liquid wall film is directly proportional to the cylinder diameter. |
Author | Xiao, Jiazhi Yang, Junwei Shen, Guoping Jin, Youhai Zhang, Xupeng |
AuthorAffiliation | Shandong Shtar Science & Technology Petrochemical Co., Ltd State Key Laboratory of Heavy Oil Processing China University of Petroleum |
AuthorAffiliation_xml | – name: China University of Petroleum – name: Shandong Shtar Science & Technology Petrochemical Co., Ltd – name: State Key Laboratory of Heavy Oil Processing |
Author_xml | – sequence: 1 givenname: Junwei surname: Yang fullname: Yang, Junwei – sequence: 2 givenname: Xupeng surname: Zhang fullname: Zhang, Xupeng – sequence: 3 givenname: Guoping surname: Shen fullname: Shen, Guoping – sequence: 4 givenname: Jiazhi surname: Xiao fullname: Xiao, Jiazhi email: xiaojiazhi@sina.com – sequence: 5 givenname: Youhai surname: Jin fullname: Jin, Youhai |
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CitedBy_id | crossref_primary_10_3389_fceng_2022_851992 crossref_primary_10_1021_acs_iecr_9b01217 crossref_primary_10_1016_j_cep_2020_107829 crossref_primary_10_1177_0954406218768838 |
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