TY - JOUR
T1 - Multi-level eco-friendly heat recovery process integrated into a gas turbine cycle of an innovative CCHP-desalination system
T2 - Assessment and optimization of the thermo-economic-environmental aspects
AU - Sui, Lu
AU - Zhou, Qili
AU - Alsenani, Theyab R.
AU - Ahmad, Sayed Fayaz
AU - Muhammad, Taseer
AU - Pourtadayyon, Mahdi
N1 - Publisher Copyright:
© 2024 Elsevier B.V.
PY - 2025/3/15
Y1 - 2025/3/15
N2 - 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.
AB - 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.
KW - CO footprint
KW - Desalination
KW - Gas turbine cycle
KW - Heat integration
KW - Hydrogen
KW - Optimization
UR - http://www.scopus.com/inward/record.url?scp=85210053610&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2024.118323
DO - 10.1016/j.desal.2024.118323
M3 - Article
AN - SCOPUS:85210053610
SN - 0011-9164
VL - 597
JO - Desalination
JF - Desalination
M1 - 118323
ER -