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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
来源:
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/).
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页码:99 / 113
页数:15
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