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Thermo-enviro-economic analysis of a novel landfill gas-fueled CCHP-desalination process combined with a liquefied natural gas cold energy recovery unit
被引:3
作者:
Xu, Zichen
[1
]
Hu, Ya-Jian
[1
]
He, Yu-Tao
[1
,2
]
Nutakki, Tirumala Uday Kumar
[3
]
Seikh, Asiful H.
[4
]
Mohanavel, V.
[5
,6
,7
]
Shah, Nehad Ali
[8
]
Qin, Muxing
[9
]
机构:
[1] Jinan Univ, Inst Adv & Appl Chem Synth, Guangzhou 510632, Peoples R China
[2] Jinan Univ, Guangdong Prov Key Lab Pharmacodynam Constituents, Guangzhou 510632, Peoples R China
[3] Amer Univ Ras Al Khaimah, RAK Res & Innovat Ctr, Ras Al Khaymah, U Arab Emirates
[4] King Saud Univ, Coll Engn, Mech Engn Dept, Riyadh 11421, Saudi Arabia
[5] Amity Univ Dubai, Dept Mech Engn, Dubai 345019, U Arab Emirates
[6] Bharath Inst Higher Educ & Res, Ctr Mat Engn & Regenerat Med, Chennai 600073, Tamil Nadu, India
[7] Chandigarh Univ, Dept Mech Engn, Mohali 140413, Punjab, India
[8] SIMATS, Saveetha Sch Engn, Dept Math, Chennai 602105, Tamilnadu, India
[9] Ton Duc Thang Univ, Fac Environm & Labour Safety, Sustainable Management Nat Resources & Environm R, Ho Chi Minh City, Vietnam
关键词:
Sustainable production;
Landfill gas;
Multi-heat recovery;
Multi-effect desalination;
Eco-friendly design;
Economic analysis;
GEOTHERMAL HEAT-SOURCE;
OPTIMIZATION;
BIOMASS;
EXERGY;
GENERATION;
PLANT;
ASSESSMENTS;
COMBUSTION;
SIMULATION;
SYSTEMS;
D O I:
10.1016/j.jclepro.2024.141675
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
This paper proposes utilizing landfill gas, obtained from landfilling activities, as a viable substitute for fossil fuels. In this study, an innovative heat design process for a landfill gas-fueled power plant is employed, representing a novel contribution to system development. The innovative cascade heat recovery process utilized in this method facilitates an eco-friendly multigeneration practice, resulting in reduced thermodynamic irreversibility and air pollution as well as an increase in the capacity of main products. Hence, the entire system consists of a bio power plant, a transcritical CO2 cycle, a low-pressure steam generation unit, a refrigeration cycle, a multi-effect desalination, and a liquefied natural gas cold utilization unit. The simulation is conducted by the Aspen HYSYS software, examining various aspects such as energy, exergy, economics, and environment. The results indicate that the energy and exergy efficiencies of the process are 79.96% and 32.93%, respectively. Moreover, the cost per unit exergy and specific CO2 emissions amount to 87.16 $/GJ and 0.2732 kg/kWh, respectively. Besides, a parametric study is performed based on the gas turbine's outlet pressure, the flue gas temperature leaving the transcritical CO2 cycle and multi-effect desalination, and the liquefied natural gas flow rate. Obtained results demonstrate that the specific CO2 emissions and cost per unit exergy face an increase with increasing the gas turbine's outlet pressure. Moreover, the increase in the flue gas temperature leaving the transcritical CO2 cycle exhibits a reduction in the CO2 emissions and an escalation in the cost per unit exergy.
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页数:20
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