Welcome to visit The Chinese Journal of Process Engineering, Today is
Flow & Transfer

Gas Pressure Drop in Gas-phase Sheared Cross-flow Rotating Packed Bed

  • YUAN Zhi-guo LIU Hui-jun LIU You-zhi
Expand
  • Shanxi Province Key Laboratory of Higee-oriented Chemical Engineering, Research Center of Shanxi Province for High Gravity Chemical Engineering and Technology, North University of China, Taiyuan, Shanxi 030051, China

Received date: 2016-11-30

  Revised date: 2017-01-10

  Online published: 2017-04-19

Abstract

Gas pressure drop was studied in Gas-phase Sheared Cross?Flow Rotating Packed Bed (GSC?RPB) by an air?water system. According to the single factor method, the effects of gas velocity, high gravity factor on dry pressure drop were examined, and the effects of gas velocity, high gravity factor and liquid spray density on wet pressure drop were investigated. The results showed that the dry pressure drop and wet pressure drop increase with the increase of gas velocity and high gravity factor. In the case of low gas velocity and big high gravity factor, the wet pressure drop decreases with the increase of liquid spray density. While in the case of high gas velocity and small high gravity factor, the wet pressure drop increases with the increase of liquid spray density. The empirical correlations for estimating the dry and wet pressure drop are proposed. The deviation of gas pressure drop predicted from the correlation is within ±15% of the experimental data.

Cite this article

YUAN Zhi-guo LIU Hui-jun LIU You-zhi . Gas Pressure Drop in Gas-phase Sheared Cross-flow Rotating Packed Bed[J]. The Chinese Journal of Process Engineering, 2017 , 17(2) : 237 -242 . DOI: 10.12034/j.issn.1009-606X.216357

References

[1]袁志国,宋卫,金国良,等.旋转填料床中种填料压降和传质特性的对比[J].化学工程, 2015, 43(7):7-11
[2]Yuan Z G, Song W, Jin G L, et al.Comparison of Pressure-drop and Mass-transfer Characteristics of Two Kinds of Packing in Countercurrent Rotating Packed Bed[J].Chemical Engineering(China), 2015, 43(7):7-11
[3]谷德银,刘有智,祁贵生,等.新型旋转填料床的气相传质特性[J].过程工程学报, 2015, 15(1):35-39
[4]Gu D Y, Liu Y Z, Qi G S, et al.Research on the Mass Transfer Characteristics of Gas Phase in a Novel Rotating Packed Bed[J].The Chinese Journal of Process Engineering, 2015, 15(1):35-39
[5]Luo Y, Chu G W, Zou H K, et al.Mass Transfer Studies in a Rotating Packed Bed with Novel Rotors: Chemisorption of CO2[J].Industrial and Engineering Chemistry Research, 2012, 51(26):9164-9172
[6]Sandilya P,Rao D P,Sharma A,et al.Gas-phase mass transfer in a centrifugal contactor[J].Industrial and Engineering Chemistry Research, 2001, 40(1):384-392
[7]Chen Y S, Liu H S.Absorption of VOCs in a rotating packed bed[J].Industrial and Engineering Chemistry Research, 2002, 41(6):1583-1588
[8]Rao D P, Bhowal A, Goswami P S.Process intensification in rotating packed beds (HIGEE): An appraisal[J].Industrial and Engineering Chemistry Research, 2004, 43(4):1150-1162
[9]祁贵生,焦纬洲,刘有智,等.新型填料结构旋转床传质特性[J].化学反应工程与工艺, 2009, 25(2):109-115
[10]Qi G S, Jiao W Z, Liu Y Z, et al.Mass Transfer Characteristics of a Rotating Packed Bed with New Type Packings[J].Chemical Reaction Engineering and Technology, 2009, 25(2):109-115
[11]Chandra A, Goswami P S, Rao D P.Characteristics of flow in a rotating packed bed (HIGEE) with split packing[J].Industrial and Engineering Chemistry Research, 2005, 44(11):4051-4060
[12] 中北大学.气流逆向剪切旋转填料床传质与反应设备:201310402588.9[P]. 2013-12-25.
[13]North University of China.The Mass Transfer and Reaction Equipment of Counter Airflow Shear Rotating Packed Bed: 201310402588.9 [P]. 2013?12?25.
[14]LinC C, Chen Y W.Performance of a cross-flow rotating packed bed in removing carbon dioxide from gaseous streams by chemical absorption[J].International Journal of Greenhouse Gas Control, 2011, 5(4):668-675
[15]Lin C C, Chen B C.Characteristics of cross-flow rotating packed beds[J].Journal of Industrial and Engineering Chemistry, 2008, 14(3):322-327
[16] 中北大学.一种多级错流旋转填料床传质与反应设备:201410672155.x[P]. 2014-04-01.
[17]North University of China.The Mass Transfer and Reaction Equipment of Multilevel Cross-flow Rotating Packed bed: 201410672155.x [P]. 2014?04?01.
[18]刘有智,刘振河,康荣灿,等.错流旋转填料床气相压降特性[J].化工学报, 2007, 58(4):869-874
[19]Liu Y Z, Liu Z H, Kan R C, et al.Characteristics of gas pressure drop in cross flow rotating packed bed[J].Journal of Chemical Industry and Engineering, 2007, 58(4):869-874
[20] 郭奋.错流旋转床内流体力学与传质特性的研究 [D]. 北京:北京化工大学, 1996.
[21]Guo F.Hydrodynamics and mass transfer in cross-flow rotating packed bed [D]. Beijing: Beijing University of Chemical Technology, 1996
[22]赵海红,刘有智,石国亮,等.错流旋转填料床气相压降特性研究[J].科技开发, 2004, 12(2):12-15
[23]Zhao H H, Liu Y Z, Shi G L, et al.Studies on gas pressure drop characteristics of cross-flow rotating packed bed[J].Science& Technology in Chemical Industry, 2004, 12(2):12-15
[24]焦纬洲,刘有智,祁贵生.新型填料结构旋转床流体力学特性[J].化学反应工程与工艺, 2009, 25(1):29-35
[25]Jiao W Z, Liu Y Z, Qi G S.Hydrodynamics Characteristics of a New Type of Packing in a Rotating Packed Bed[J].Chemical Reaction Engineering and Technology, 2009, 25(1):29-35
[26]刘振河,刘有智,焦纬洲, 等.错流旋转填料床气相压降的研究[J].化学反应工程与工艺, 2006, 22(5):451-456
[27]Liu Z H, Liu Y Z, Jiao W Z, et al.Study on Pressure Drop in Cross Flow Rotating Packed Bed[J].Chemical Reaction Engineering and Technology, 2006, 22(5):451-456
[28] 王焕,祁贵生,刘有智,等. .错流旋转填料床气相压降特性实验研究[J].天然气化工(C1化学与化工), 2013, 38(6):38-41
[29]Wang H, Qi G S, Liu Y Z, et al.Characteristics of gas pressure drop of a cross-flow rotating packed bed[J].Natural Gas Chemical Industry, 2013, 38(6):38-41
[30] Wei Z J, You Z L, Gui S Q.Gas Pressure Drop and Mass Transfer Characteristics in a Cross-flow Rotating Packed Bed with Porous Plate Packing [J].American Chemical Society, 2010, 49(8):3732-3740
Outlines

/