Thermoeconomic modeling of new energy system based on biogas upgrading to multigenerational purpose

被引:1
|
作者
Wu, Yuwen [1 ]
机构
[1] Fujian Normal Univ, Coll Math & Stat, Fuzhou, Fujian, Peoples R China
关键词
Multigeneration; Exergy; Energy; Cost of exergy unit; Desalination; Biogas upgrading; LNG regasification; GEOTHERMAL HEAT-SOURCE; GAS-TURBINE; MULTICRITERIA OPTIMIZATION; HYDROGEN-PRODUCTION; SUPERCRITICAL CO2; EXERGY ANALYSIS; POWER-PLANT; FRESH-WATER; DRIVEN; CYCLE;
D O I
10.1016/j.desal.2024.118215
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The following article outlines an integrated approach toward the valorization of biogas for energy, chilled water, hot water, freshwater, and liquid carbon dioxide production. The suggested system includes a biogas upgrading unit with a biomethane-fueled burner, a Kalian cycle, an LNG regasification process, and a multi-effect desalination unit that can provide CO2, electricity, cooling, and heating. The new ideas in the proposed system include a cryogenic biogas upgrading process that can be used in many industrial settings, the production of liquid carbon dioxide through biogas upgrading, and the use of biomethane in the integrated combustion process. Furthermore, the grey wolf optimization technique is applied in various multi-objective optimization contexts to achieve optimal operating conditions and preferred performance outcomes. In this simulation, the generation of electricity reaches a value of 755 kW. Attached to it is a cooling load of about 5102 kW, with a heating load of 4725 kW, freshwater capacity about 1.33 kg/s, production rate of liquid CO2 at 0.58 kg/s, and natural gas at 3.1 kg/s. Thermodynamic results reveal that the proposed multigeneration performance scheme providently enhances energy and exergy efficiencies up to 59.82 % and 5.74 %, respectively, compared to the condition of a single product. The performed exergy analysis shows that the overall irreversibility of the suggested configuration is equal to 18,047 kW while about 42.6 % of this value is contributed from the heat exchanger E-104. Moreover, the CO2 emission intensity of the process can be kept as 0.35 kg/kWh. Cryogenic separation can obtain about 88 % of CO2 in biogas and turn it into its liquid phase. The performed economic assessment has resulted in the following total cost rate as well as cost per unit exergy: 321.38 $/h and 83.06 $/GJ, respectively. Under optimal conditions, an exergy efficiency of 13.40 % and a net power output of 2034.39 kW are attained.
引用
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页数:24
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