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Investigating influences of geometric factors on a solar thermochemical reactor for two-step carbon dioxide splitting via CFD models
被引:13
|作者:
Zhang, Han
[1
]
Smith, Joseph D.
[1
]
机构:
[1] Missouri Univ Sci & Technol, Dept Chem & Biochem Engn, 210C,Bertelsmeyer Hall,1101 North State St, Rolla, MO 65409 USA
来源:
关键词:
Solar energy;
Solar thermochemical reactor;
Radiative transfer;
DEM;
CeO2;
reduction;
HYDROGEN-PRODUCTION;
SYNGAS PRODUCTION;
HEAT-TRANSFER;
METHANE;
WATER;
GASIFICATION;
BIOMASS;
ENERGY;
IMPROVEMENT;
EFFICIENCY;
D O I:
10.1016/j.solener.2019.06.080
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:
Solar thermochemical processes utilize inexhaustible solar energy as a thermal driving force to provide heat and motivate reactions, which offer pathways to store solar energy as chemical fuels. Some elevated temperature reactions, like thermal decomposition, gasification, and methane reforming, are anticipated in solar reactors which have the ability to provide extremely high temperatures. Presently, the dominating considerations in the design of solar reactors are heat and mass transfer with reaction mechanisms. A novel partition cavity-receiver reactor concept is proposed in this paper. In order to provide a longer pathway of interaction between the catalyst and reactants, a partition is introduced in this cavity-receiver reactor. A numerical computational fluid dynamics (CF-D) analysis is performed to study the influences of geometric factors (i.e. gap size between partition and bottom, inlets/outlets position, catalyst thickness) under both uniform and model-generated distribution of concentrated radiant fluxes. A two-step solar thermochemical redox reaction using ceria as a catalyst to split CO2 is modeled in the partition cavity-receiver reactor to investigate the relationship between geometric factors and reaction rates. Based on the comparisons and analysis of results, optimized geometric factors and corresponding operating conditions are discussed.
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页码:935 / 950
页数:16
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