Multi-level eco-friendly heat recovery process integrated into a gas turbine cycle of an innovative CCHP-desalination system: Assessment and optimization of the thermo-economic-environmental aspects

被引:0
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作者
Sui, Lu [1 ,2 ]
Zhou, Qili [3 ]
Alsenani, Theyab R. [4 ]
Ahmad, Sayed Fayaz [5 ]
Muhammad, Taseer [6 ]
Pourtadayyon, Mahdi [7 ]
机构
[1] School of Finance, Shandong Technology and Business University, China
[2] Shandong Xixiakou Haizhen Co., Ltd, China
[3] School of Finance and Economics, Nanchang Institute of Technology, China
[4] Department of Electrical Engineering, College of Engineering in Al-Kharj, Prince Sattam Bin Abdulaziz University, Al-Kharj,11942, Saudi Arabia
[5] Department of Engineering Management, Institute of Business Management, Karachi, Pakistan
[6] Department of Mathematics, College of Science, King Khalid University, Abha,61413, Saudi Arabia
[7] Sustainable Management of Natural Resources and Environment Research Group, Faculty of Environment and Labour Safety, Ton Duc Thang University, Ho Chi Minh City, Viet Nam
关键词
Absorption cooling - Absorption refrigeration - Desalination - Gas turbines - Kyoto Protocol - Seawater - Waste heat - Water filtration;
D O I
10.1016/j.desal.2024.118323
中图分类号
学科分类号
摘要
Concerning the high energy loss associated with benchmark gas turbine cycles and relative irreversibility, research on how this drawback can be controlled and managed for long-term sustainability, enhanced performance, and declined emissions of greenhouse gases is essential. In this context, a novel multi-level thermal recovery method is designed and introduced for a gas turbine cycle, aimed at simultaneously yielding electricity, hot and chilled water, hydrogen, and desalinated water. The planned setup encompasses an ammonia Rankine cycle, an organic Rankine cycle, an absorption chiller, a desalination unit, and a proton exchange membrane electrolyzer, resulting in reduced irreversibility and emissions. The system's capability is examined concerning exergy, energy, environmental, and economic aspects using Aspen HYSYS software. Furthermore, a comparative study is conducted between different optimization scenarios. According to the attained outcomes, maximizing vapor production requires a reduction in seawater flow. Additionally, increasing the seawater flow rate is ineffective in the proposed process, as vapor from the desalination unit drives heat transfer. Regarding the optimizations conducted, the most suitable exergy efficiency is found to be 39.27 %, which corresponds to the exergy-power scenario. Moreover, the optimal net electric power, and cooling and heating loads are calculated at 18,255 kW, 4383 kW, and 15,280 kW, respectively; thus, the optimal energy efficiency is 74.51 %. From economic and environmental perspectives, the optimal cost of energy and CO2 footprint are 0.76 $/kWh and 0.255 kg/kWh, correspondingly. © 2024 Elsevier B.V.
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