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Multigeneration-CAES system with biomass energy integration: Energy implications and exergoeconomic
被引:0
|作者:
Rahmanian, Shayan
[1
]
Safari, Hediyeh
[1
,2
]
Soltani, M.
[1
,2
,3
,4
,6
]
Dusseault, M. B.
[5
]
机构:
[1] KN Toosi Univ Technol, Dept Mech Engn, Tehran 1996715433, Iran
[2] Univ Waterloo, Dept Elect & Comp Engn, Waterloo, ON N2L 3G1, Canada
[3] Univ Waterloo, Waterloo Inst Sustainable Energy WISE, Waterloo, ON N2L 3G1, Canada
[4] Int Business Univ, Ctr Sustainable Business, Toronto, ON, Canada
[5] Univ Waterloo, Dept Earth & Environm Sci, Waterloo, ON N2L 3G1, Canada
[6] Balsillie Sch Int Affairs BSIA, Waterloo, ON, Canada
关键词:
Renewable energy;
Multigeneration system (MGS);
Biomass energy;
Proton exchange membrane (PEM) electrolysis;
Compressed air energy storage (CAES);
GEOTHERMAL HEAT-SOURCE;
HYDROGEN-PRODUCTION;
EXERGY ANALYSIS;
GAS-TURBINE;
MULTIOBJECTIVE OPTIMIZATION;
PEM ELECTROLYZER;
POWER;
DRIVEN;
PERFORMANCE;
WATER;
D O I:
10.1016/j.est.2024.111851
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:
Using biomass energy, this research evaluated the energy, exergy and exergoeconomic characteristics of the combination of the multigeneration system (MGS) and the compressed air energy storage system (CAES). It features a combined Brayton and compressed air energy storage sub-cycle (CBACS) and a combined proton exchange membrane (PEM) electrolysis and heating sub-cycle (CPEAHS). Hot water is generated economically during off-peak hours, while electricity, hot water, hydrogen, and oxygen are generated during peak hours. Through evaluating the system's charge/discharge, it was found that the MGS-CAES can produce 681 kW of electricity, 5.8 kg/s of hot water, 5.4 kg/h of hydrogen, and 6.7 kg/h of oxygen, making its implementation feasible. As part of our parametric study, we explored how decision variables, including the entry temperature of the gas turbine, the entry pressure of the compressed air storage cavern (CASC), the CASC outlet pressure and biomass mass flow rate affect thermal and economic performance. Upon lowering the entry temperature of the gas turbine, the round-trip productivity increased by 1.1 %, and the overall capital investment and overall cost of the product were both reduced to 85.8 $/h and 111 $/h. The exergy destruction cost rate reaches its minimum value of $ 64.24 per hour at an inlet pressure of 2200 kPa for the CASC system., while rising the CASC outlet pressure improved the MGS-CAES exergy round trip efficiency by 3.4 %. It is estimated that biomass mass flow rate growth resulted in an enhancement of heat and electricity production.
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页数:17
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