SCI和EI收录∣中国化工学会会刊

›› 2010, Vol. 18 ›› Issue (2): 249-257.

• CATALYSIS, KINETICS AND REACTOR • Previous Articles     Next Articles

Modeling of the Precipitation Process in a Rotating Packed Bed and Its Experimental Validation

XIANG Yang1, WEN Lixiong1,2, CHU Guangwen1, SHAO Lei1,2, XIAO Guangting2, CHEN Jianfeng1,2   

  1. 1. Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology, Beijing 100029, China;
    2. Key Laboratory for Nanomaterials, Ministry of Education, Beijing University of Chemical Technology, Beijing 100029, China
  • Received:2009-07-14 Revised:2010-02-10 Online:2010-04-28 Published:2010-04-28
  • Supported by:
    Supported by the National Natural Science Foundation of China(20821004,20325621);Beijing Municipal Commission of Education(JD100100403)

Modeling of the Precipitation Process in a Rotating Packed Bed and Its Experimental Validation

向阳1, 文利雄1,2, 初广文1, 邵磊1,2, 肖光庭2, 陈建峰1,2   

  1. 1. Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology, Beijing 100029, China;
    2. Key Laboratory for Nanomaterials, Ministry of Education, Beijing University of Chemical Technology, Beijing 100029, China
  • 通讯作者: CHEN Jianfeng,E-mail:chenjf@mail.buct.edu.cn
  • 基金资助:
    Supported by the National Natural Science Foundation of China(20821004,20325621);Beijing Municipal Commission of Education(JD100100403)

Abstract: A mixing-precipitation model based on the modified coalescence-redispersion model was presented to describe the flow,mixing,nucleation and growth in a rotating packed bed(RPB).The model was coupled with population balance,mass balance and crystallization kinetics.It predicted well the influence of coalescence prob-ability,which represents the mixing intensity among droplets,on the particle number density,supersaturation and mean particle size of the produced precipitates.The effects of the radial thickness of packing,liquid flow rate and rotating speed on the product particle size were also investigated.The results indicate that the needed radial length of packing is short for sparingly soluble substance precipitation(about 40-50 mm in this work), and the mean parti-cle size of precipitates decreases with the increase of rotating speed and liquid flow rate,respectively.The validity of this model was verified by experiment on BaSO4 precipitation in RPB.

Key words: rotating packed bed, precipitation, BaSO4, coalescence-redispersion model, mixing

摘要: A mixing-precipitation model based on the modified coalescence-redispersion model was presented to describe the flow,mixing,nucleation and growth in a rotating packed bed(RPB).The model was coupled with population balance,mass balance and crystallization kinetics.It predicted well the influence of coalescence prob-ability,which represents the mixing intensity among droplets,on the particle number density,supersaturation and mean particle size of the produced precipitates.The effects of the radial thickness of packing,liquid flow rate and rotating speed on the product particle size were also investigated.The results indicate that the needed radial length of packing is short for sparingly soluble substance precipitation(about 40-50 mm in this work), and the mean parti-cle size of precipitates decreases with the increase of rotating speed and liquid flow rate,respectively.The validity of this model was verified by experiment on BaSO4 precipitation in RPB.

关键词: rotating packed bed, precipitation, BaSO4, coalescence-redispersion model, mixing