Economic examination and multi-objective optimization of integrating a novel geothermal-driven combined cooling and power (CCP) system using a bi-evaporator cycle with a low-temperature electrolyzer

被引:11
作者
Cao, Yan [1 ]
Dhahad, Hayder A. [2 ]
El-Shafay, A. S. [3 ]
Ahmed, Ahmed Najat [4 ]
Mohamed, Abdullah [5 ]
Almojil, Sattam Fahad [6 ]
Almohana, Abdulaziz Ibrahim [6 ]
Alali, Abdulrhman Fahmi [6 ]
机构
[1] Xian Technol Univ, Sch Mechatron Engn, Xian 710021, Peoples R China
[2] Univ Technol Baghdad, Mech Engn Dept, Baghdad, Iraq
[3] Prince Sattam Bin Abdulaziz Univ, Coll Engn, Dept Mech Engn, Alkharj 16273, Saudi Arabia
[4] Lebanese French Univ, Coll Engn & Comp Sci, Dept Comp Engn, Kurdistan Region, Iraq
[5] Future Univ Egypt, Res Ctr, New Cairo 11745, Egypt
[6] King Saud Univ, Coll Engn, Dept Civil Engn, POB 800, Riyadh 11421, Saudi Arabia
关键词
Combined cooling and power; Geothermal; Hydrogen; Bi-evaporator; Multi-objective optimization; Dual parametric study; HEAT-PUMP SYSTEM; WATER PRODUCTION; MULTIGENERATION SYSTEM; TRIGENERATION SYSTEM; WORKING FLUIDS; HYDROGEN; ENERGY; FLASH; EXERGY; PLANT;
D O I
10.1016/j.ijhydene.2022.04.105
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
Concerning substantial waste heat in geothermal cycles, this study suggests and investigates the feasibility of a novel framework of waste heat recovery for a double-flash binary geothermal cycle. In this manner, a novel design of an ejector-based bi-evaporator technology is configured and integrated with the geothermal cycle. For better applicability, a low-temperature electrolyzer, i.e., proton exchange membrane electrolyzer (PEME), is joined to the whole configuration producing electricity, cooling, and hydrogen simultaneously. This arrangement is analyzed from the exergy and cost viewpoints using the engineering equation solver (EES) software and is optimized coupling EES and MATLAB programming. A non-dominated sorting genetic algorithm (NSGA-II) optimization method is utilized by which the objective functions, i.e., exergy efficiency and sum unit cost of products, are computed at 40.3% and 6.9 $/GJ, respectively. Additionally, the optimum values of the produced electricity, cooling, and hydrogen are correspondingly equal to 4.29 MW, 1.90 MW, and 4.51 kg/h. In the optimum state, the major irreversibility source is ejector 1 with a 16.8% contribution to the total exergy destruction rate (= 5745.7 kW). Furthermore, turbine 1 is the expensive component among the established devices with a 22.3% contribution to the total investment cost rate (= 172.3 $/h). (C) 2022 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:19955 / 19976
页数:22
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