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
收藏
页数:24
相关论文
共 50 条
  • [1] Energy and exergy analyses of a biogas driven multigenerational system
    Sevinchan, Eren
    Dincer, Ibrahim
    Lang, Haoxiang
    ENERGY, 2019, 166 : 715 - 723
  • [2] Biogas desulfurization and biogas upgrading using a hybrid membrane system - modeling study
    Makaruk, A.
    Miltner, M.
    Harasek, M.
    WATER SCIENCE AND TECHNOLOGY, 2013, 67 (02) : 326 - 332
  • [3] Thermoeconomic Analysis of an Innovative Integrated System for Cogeneration of Liquid Hydrogen and Biomethane by a Cryogenic-Based Biogas Upgrading Cycle and Polymer Electrolyte Membrane Electrolysis
    Ghorbani, Bahram
    Zendehboudi, Sohrab
    Saady, Noori M. Cata
    Azarpour, Abbas
    Albayati, Talib M.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2024, 63 (16) : 7227 - 7257
  • [4] Thermoeconomic modeling and optimization of a hydrogen production system using geothermal energy
    Yilmaz, Ceyhun
    GEOTHERMICS, 2017, 65 : 32 - 43
  • [5] A new multigenerational solar-energy based system for electricity, heat and hydrogen production
    Franzese, Nicola
    Dincer, Ibrahim
    Sorrentino, Marco
    APPLIED THERMAL ENGINEERING, 2020, 171 (171)
  • [6] High efficiency in-situ biogas upgrading in a bioelectrochemical system with low energy input
    Liu, Chuanqi
    Xiao, Jiewen
    Li, Haoyong
    Chen, Qian
    Sun, Dezhi
    Cheng, Xiang
    Li, Pengsong
    Dang, Yan
    Smith, Jessica A.
    Holmes, Dawn E.
    WATER RESEARCH, 2021, 197
  • [7] Thermoeconomic assessment of a novel integrated CHP system incorporating solar energy based biogas-steam reformer with methanol and hydrogen production
    Mosaffa, A. H.
    Ghaffarpour, Z.
    Farshi, L. Garousi
    SOLAR ENERGY, 2019, 178 : 1 - 16
  • [8] An integrated thermoeconomic modeling and optimization strategy for aircraft/aerospace energy system design
    Muñoz, JR
    von Spakovsky, MR
    OCOS 2000: FROM THERMO-ECONOMICS TO SUSTAINABILITY, PTS 1-4, 2000, : 79 - 111
  • [9] Energy management strategy for a biogas plant in Anhui, China based on waste heat recovery and thermoeconomic analysis
    Lu, Fulu
    Pan, Chuhan
    Zhu, Hongguang
    Pan, Fanghui
    Wu, Qi
    ENERGY CONVERSION AND MANAGEMENT, 2022, 273
  • [10] Energy Based Thermoeconomic Analysis of a Combined Cycle System with Steam Extraction (Cogeneration System)
    Cetin, Burhanettin
    Erdem, Hasan Huseyin
    Sevilgen, Suleyman Hakan
    ADVANCES IN MECHANICAL ENGINEERING, 2014,