Innovative Internally Circulating Reactor Concept for Chemical Looping-Based CO2 Capture Processes: Hydrodynamic Investigation

被引:18
|
作者
Zaabout, Abdelghafour [1 ]
Cloete, Schalk [1 ]
Amini, Shahriar [1 ]
机构
[1] SINTEF Mat & Chem, Flow Technol Dept, SP Andersens Veg 15 B, N-7034 Trondheim, Norway
关键词
Chemical looping; CO2; capture; Fluidized bed; Gas leakage; Hydrodynamics; SWITCHING COMBUSTION REACTOR; FLUIDIZED-BED REACTOR; SOLID CIRCULATION; POWER PRODUCTION; SYSTEM; GENERATION; SEPARATION; MIXTURES; HYDROGEN; FUEL;
D O I
10.1002/ceat.201500222
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An experimental hydrodynamic investigation has been carried out for a novel internally circulating chemical looping (ICCL) reactor concept proposed to reduce the technical complexities encountered in conventional chemical looping combustion (CLC) and reforming (CLR) technologies. The concept consists of a single reactor with internal physical separations dividing it into two sections, i.e., the fuel and air sections. The trade-off for this reduction in process complexity is increased gas leakage between the two reactor sections, so a pseudo-2D cold-flow experimental unit was designed. The ICCL concept remains highly efficient in terms of CO2 separation while ensuring significant process simplifications. The solids circulation rate also proved easy to control by adjusting the fluidization velocity ratio and the bed loading. In the light of the excellent hydrodynamic performance, the ICCL concept appears to be well-suited for further development as a CLC/CLR reactor model.
引用
收藏
页码:1413 / 1424
页数:12
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