Autothermal hybridization and controlled production of hydrogen-rich syngas in a molten salt solar gasifier

被引:14
|
作者
Hathaway, Brandon J. [1 ,2 ]
Davidson, Jane H. [1 ]
机构
[1] Univ Minnesota, Dept Mech Engn, 111 Church St SE, Minneapolis, MN 55455 USA
[2] Sunvapor Inc, Pasadena, CA USA
关键词
Solar; Gasification; Hybridization; Autothermal; Biomass; Molten salt; CIRCULATING FLUIDIZED-BED; STEAM-GASIFICATION; REACTOR EXPERIMENTATION; COAL COKES; BIOMASS; POWER; DESIGN; ENERGY;
D O I
10.1016/j.ijhydene.2021.02.048
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
High efficiency solar steam gasification of biomass is carried out in a prototype molten salt reactor for solar-only and solar-autothermal hybrid operation. Previous demonstration of the prototype 3-kW solar gasifier for steam gasification of cellulose at stoichiometric conditions demonstrated thermal efficiency of 44% during continuous operation at 1200 K. The present work expands the range of operating conditions to consider two challenges. Hybridization between solar and autothermal modes of operation is accomplished by adding oxygen directly to the reactor. Control of the H-2:CO ratio of the product gas is accomplished through in-situ steam shifting. Hybridization stabilized temperatures for variations in radiative input as large as a 30% reduction in power, corresponding to conditions where both sensible and chemical heat demands for the process were fully met by exothermic heat release with no significant challenges. Peak efficiencies and carbon conversion values observed are 45% and 99.5% respectively. The resulting product gas stream composition was shifted from a hydrogen and carbon monoxide ratio of 1:1 with stoichiometric steam delivery to a ratio of 1.7:1 with steam at nine times the stoichiometric amount, only slightly lower than equilibrium predictions. The results demonstrate-very favorable attributes for the molten salt reactor in a continuous fuel production process. (C) 2021 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:15257 / 15267
页数:11
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