A comprehensive multi-variable approach for evaluating the feasibility of integration a novel heat recovery model into a gas turbine power plant, producing electricity, heat, and methanol

被引:1
作者
Tan, Hua [1 ]
Bo, Likang [1 ]
Nutakki, Tirumala Uday Kumar [2 ]
Agrawal, Manoj Kumar [3 ]
Seikh, Asiful H. [4 ]
Chauhdary, Sohaib Tahir [5 ]
Shah, Nehad Ali [6 ]
Ji, Tiancheng [7 ]
机构
[1] Hebei Vocat Univ Technol & Engn, Elect Engn, Tianjin 054000, Hebei, Peoples R China
[2] Amer Univ Ras Al Khaimah, RAK Res & Innovat Ctr, Ras Al Khaymah, U Arab Emirates
[3] GLA Univ, Mathura 281406, UP, India
[4] King Saud Univ, Coll Engn, Mech Engn Dept, Riyadh 11421, Saudi Arabia
[5] Dhofar Univ, Coll Engn, Dept Elect & Comp Engn, Salalah 211, Oman
[6] SIMATS, Saveetha Sch Engn, Dept Math, Chennai 602105, Tamilnadu, India
[7] Ton Duc Thang Univ, Fac Environm & Labour Safety, Sustainable Management Nat Resources & Environm Re, Ho Chi Minh City, Vietnam
关键词
Thermal integration; Gas turbine cycle; Eco-friendly process; Aspen HYSYS; Multi -variable assessment; Methanol; LNG COLD ENERGY; MULTIGENERATION SYSTEM; BIOMASS GASIFICATION; EXERGY ANALYSIS; CARBON-DIOXIDE; FUEL-CELL; OPTIMIZATION; PERFORMANCE; CYCLE; SIMULATION;
D O I
10.1016/j.energy.2024.131145
中图分类号
O414.1 [热力学];
学科分类号
摘要
Considering the importance of efficient thermal integration for a gas turbine cycle using its energetic flue gas, the current paper proposes an eco-friendly and efficient process integrated into a gas turbine cycle. The newly designed polygeneration structure produces power, hot water, and methanol. The components of this system include a heat provider unit, a direct carbon dioxide hydrogenation unit for the production of methanol, an ammonia Rankine cycle, a proton exchange membrane electrolyzer, a supercritical carbon dioxide power cycle, and two organic Rankine cycles. The feasibility of the proposed model is evaluated using a comprehensive multivariable assessment from energy, exergy, economic, and environmental approaches. This system exhibits a power production capacity of 17197.23 kW and a methanol generation rate of 0.7573 kg/s. Also, the total irreversibility is equal to 68161.18 kW. Besides, the total energy and exergy efficiencies are found as 68.73% and 32.03%, respectively. This model's carbon dioxide emission is 18667.36 kgCO2/h, and its carbon footprint equals 0.2196 kgCO2/kWh. Furthermore, the economic analysis reveals that the project has an annual total cost of 194,602,338 and a net present value of 686,221,616. Besides, the computed total unit costs for products and energy are 0.3385 $/kWh and 89.81 $/GJ, respectively.
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页数:14
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