Chemical and thermal performance analysis of a solar thermochemical reactor for hydrogen production via two-step WS cycle

被引:6
|
作者
Sharma, Jeet Prakash [1 ]
Kumar, Ravinder [1 ]
Ahmadi, Mohammad H. [2 ]
Mukhtar, Azfarizal [3 ]
Yasir, Ahmad Shah Hizam Md [4 ]
Sharifpur, Mohsen [5 ,6 ]
Ongar, Bulbul [7 ]
Yegzekova, Anara [8 ]
机构
[1] Lovely Profess Univ, Sch Mech Engn, Phagwara 144411, Punjab, India
[2] Shahrood Univ Technol, Fac Mech Engn, Shahrood, Iran
[3] Univ Tenaga Nas, Inst Sustainable Energy, Putrajaya Campus,Jalan IKRAM UNITEN, Kajang 43000, Malaysia
[4] Rabdan Acad, 65 Al Inshirah,POB 114646, Abu Dhabi 22401, U Arab Emirates
[5] Univ Pretoria, Dept Mech & Aeronaut Engn, ZA-0002 Pretoria, South Africa
[6] China Med Univ, China Med Univ Hosp, Dept Med Res, Taichung, Taiwan
[7] Satbayev Univ, Dept Power Engn, 22a Satpaev Str, Alma Ata 050013, Kazakhstan
[8] Logist & Transport Acad, Dept Power Engn, 97 Shevchenko Str, Alma Ata 050012, Kazakhstan
关键词
STCR modelling; Porous media; Thermal analysis; Solar fuels; WS process; SolTrace; PARABOLIC DISH; CAVITY RECEIVER; HEAT-TRANSFER; NUMERICAL-SIMULATION; THEORETICAL-ANALYSIS; OPTICAL-PERFORMANCE; CYLINDRICAL CAVITY; FUEL PRODUCTION; SYSTEM; RADIATION;
D O I
10.1016/j.egyr.2023.06.012
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
Ceria-based H2O/CO2-splitting solar-driven thermochemical cycle produces hydrogen or syngas. Thermal optimization of solar thermochemical reactor (STCR) improves the solar-to-fuel conversion efficiency. This research presents two conceptual designs and thermal modelling of RPC-ceria-based STCR cavities to attain the optimal operating conditions for CeO2 reduction step. Presented hybrid geometries consisting of cylindrical-hemispherical and conical frustum-hemispherical structures. The focal point was positioned at x = 0, -10 mm, and -20 mm from the aperture to examine the flux distribution in both solar reactor configurations. Case-1 with 2 milliradian S.E (slope error) yields a 27% greater solar flux than case-1 with 4 milliradians S.E, despite the 4 milliradian S.E produces an elevated temperature in the reactor cavity. The mean temperature in the reactive porous region was most significant for case-2 (x = -10 mm) with 4 mrad S.E for model-2, reaching 1966 K and 2008 K radially and axially, respectively. In case-2 (x = -10 mm) for 4 mrad S.E, model-1 attained 1720 K. The efficiency analysis shows that the highest conversion efficiency value was obtained to be 7.95% for case-1 with 4 milliradian S.E.& COPY; 2023 The Author(s). Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
引用
收藏
页码:99 / 113
页数:15
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