Countercurrent gas-solid trickle flow reactor with structured packing: Hydrodynamics and CaO-CO2 reaction

被引:3
作者
Obradovic, Ana [1 ]
Levec, Janez [1 ,2 ]
机构
[1] Natl Inst Chem, Lab Catalysis & Chem React Engn, Ljubljana 1000, Slovenia
[2] Univ Ljubljana, Fac Chem & Chem Technol, Ljubljana 1000, Slovenia
关键词
CaO-CO2; reaction; hydrodynamics; countercurrent gas-solid trickle flow; structured packing; plug flow model; RANDOM PORE MODEL; PRODUCT LAYER; CO2; CAPTURE; CARBONATION/CALCINATION; CAO; CARBONATION; DIFFUSION; PARTICLES; LIMESTONE; CATALYST;
D O I
10.1002/aic.14731
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The sorption reaction CaO-CO2 was examined in a countercurrent gas-solid trickle flow reactor with regularly stacked packing at T=500-600 degrees C, p(CO2)=40-50 kPa, solid-phase fluxes S=0.3-0.5 kg m(-2) s(-1), and CaO particles of 500-710 m in size. Sorption kinetics was evaluated by thermogravimetric (TG) technique. The random pore model was used for the description of the carbonization reaction. Hydrodynamic characteristics of gas-solid trickle flow were estimated at room temperature and ambient pressure. Plug flow model of both gas and solid-phase, with the parameters obtained from TG and hydrodynamics experiments, satisfactorily described the sorption process in countercurrent gas-solid trickle flow reactor. (c) 2015 American Institute of Chemical Engineers AIChE J, 61: 1601-1612, 2015
引用
收藏
页码:1601 / 1612
页数:12
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