A comprehensive thermo-economic-environmental study of an eco-friendly process incorporated with a natural gas-fed combined power plant for a novel multigeneration application
In order to achieve very efficient heat recovery, this study presents an innovative, environmentally friendly multigeneration process that is incorporated into a natural gas combined cycle system. A water electrolyzer, an enhanced absorption refrigeration cycle, a water desalination unit, and methan...
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Veröffentlicht in: | Journal of cleaner production 2024-01, Vol.434, p.139959, Article 139959 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | In order to achieve very efficient heat recovery, this study presents an innovative, environmentally friendly multigeneration process that is incorporated into a natural gas combined cycle system. A water electrolyzer, an enhanced absorption refrigeration cycle, a water desalination unit, and methanol production are only a few of the subsystems that must be used in this process. The simulation methods are carried out using the Aspen HYSYS program, which allows for a comprehensive study about the thermo-economic-environmental component. The feasibility analysis results show that the system can produce 111 MW of electricity, 175.6 kg/s of chilled water, 334.9 kg/s of domestic hot water, 7.54 kg/s of oxygen, 18.8 kg/s of fresh water, and 4.59 kg/s of methanol. Consequently, it is found that the energy and energy efficiencies are, respectively, 55.58% and 62.36%. It is shown that 344.3 MW is the overall irreversibility related to the suggested construction. Notably, the combustion chamber contributes the most of all the components, making up a significant 42.94% of the total. The primary cause of irreversibility among the subsystems is the natural gas combined cycle, which accounts for 76% of the total. Furthermore, from an economic standpoint, the entire product cost is 0.0566 $/kWh, but the total unit cost of the goods is 3.59 $/GJ. Additionally, 807.98 M$ is the determined number for the net present value. Furthermore, the suggested system has a carbon dioxide footprint of 0.286 kgCO2/kWh. This variable is 8.88% and 8.13% less than those of stand-alone power plants powered by natural gas and oil, respectively.
•Proposal and process development based on a natural gas-def combine power plant.•Generating cooling, heat, electricity, fresh water, oxygen, and methanol simultaneously.•Using Aspen HYSYS for simulation and performing 4 E study.•Exergy efficiency and CO2 footprint are equal to 62.36% and 0.286 kgCO2/kWh.•Increasing the H2-to-CO2 ratio results in an increase in methanol production. |
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ISSN: | 0959-6526 1879-1786 |
DOI: | 10.1016/j.jclepro.2023.139959 |