Numerical modeling and optimization of an entrained particle-flow thermochemical solar reactor for metal oxide reduction

被引:4
作者
Muthusamy, J. P. [1 ]
Abanades, S. [2 ]
Shamim, T. [1 ]
Calvet, N. [1 ]
机构
[1] Masdar Inst Sci & Technol, Dept Mech & Mat Engn, Inst Ctr Energy iEnergy, Abu Dhabi, U Arab Emirates
[2] PROMES CNRS, Proc Mat & Solar Energy Lab, F-66120 Font Romeu, France
来源
INTERNATIONAL CONFERENCE ON CONCENTRATING SOLAR POWER AND CHEMICAL ENERGY SYSTEMS, SOLARPACES 2014 | 2015年 / 69卷
关键词
thermochemical; solar reactor; reactive particle laden flow; thermal dissociation; CFD; metal oxide; redox; HYDROGEN-PRODUCTION; CHEMICAL REACTOR; THERMAL-DISSOCIATION; TEMPERATURE; DESIGN; RECEIVER;
D O I
10.1016/j.egypro.2015.03.178
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The endothermic thermochemical process of metal oxide reduction in an indirectly-irradiated particle-laden flow solar reactor was modeled and analyzed using computational fluid dynamics (CFD) tool Ansys-Fluent. CFD modeling includes chemically reactive multiphase flow including solid-gas interactions, radiation heat transfer among particles, inner reactor walls and gas phase, and particle surface reaction chemical kinetics. A novel indirect heating cavity-type tubular solar reactor designed for continuous metal oxide reduction was simulated for predicting the temperature distribution profiles and benchmarked with onsun testing results under similar conditions. Further, design optimization on cavity size was performed for the targeted reaction temperature with enhanced handling capacity. A 50 mm cavity height was found to be suited for required temperature of above 1900 K for zinc oxide thermal reduction. Prior to reaction kinetics implementation, the study of inert particle case was carried out to understand the influence of particle heating on thermal profile. Finally, reactive particle-laden flow was simulated using Eulerian-Lagrangian combined approach. The chemical conversion efficiency of the ZnO reduction process and the solar-to-chemical energy conversion efficiency were also calculated for varied inlet particle mass flow rates. (C) 2015 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:947 / 956
页数:10
相关论文
共 20 条
[1]   Design and simulation of a solar chemical reactor for the thermal reduction of metal oxides: Case study of zinc oxide dissociation [J].
Abanades, Stephane ;
Charvin, Patrice ;
Flamant, Gilles .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (22) :6323-6333
[2]  
Abanades S, 2006, ENERGY, V31, P2805, DOI 10.1016/j.energy.2005.11.002
[3]  
ANSYS, FLUENT US DOC
[4]   RECEIVER REACTOR CONCEPTS FOR THERMOCHEMICAL TRANSPORT OF SOLAR-ENERGY [J].
DIVER, RB .
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME, 1987, 109 (03) :199-204
[5]  
Koepf E, 2012, INT J HYDROGEN ENERG, V37, P16871, DOI 10.1016/j.ijhydene.2012.08.086
[6]   Design and operation of a solar-driven thermogravimeter for high temperature kinetic analysis of solid-gas thermochemical reactions in controlled atmosphere [J].
Leveque, Gael ;
Abanades, Stephane .
SOLAR ENERGY, 2014, 105 :225-235
[7]   Review of the Two-Step H2O/CO2-Splitting Solar Thermochemical Cycle Based on Zn/ZnO Redox Reactions [J].
Loutzenhiser, Peter G. ;
Meier, Anton ;
Steinfeld, Aldo .
MATERIALS, 2010, 3 (11) :4922-4938
[8]   Modeling of a novel high-temperature solar chemical reactor [J].
Meier, A ;
Ganz, J ;
Steinfeld, A .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (11) :3181-3186
[9]   A cavity-receiver containing a tubular absorber for high-temperature thermochemical processing using concentrated solar energy [J].
Melchior, Tom ;
Perkins, Christopher ;
Weimer, Alan W. ;
Steinfeld, Aldo .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2008, 47 (11) :1496-1503
[10]   The development of a solar chemical reactor for the direct thermal dissociation of zinc oxide [J].
Möller, S ;
Palumbo, R .
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME, 2001, 123 (02) :83-90