Thermodynamic analysis of poly-generation system for gas-biochar-heat-electricity based on supercritical water gasification of biomass waste

被引:1
|
作者
Wang, Cui [1 ,2 ,3 ,4 ,5 ]
Jin, Hui [4 ]
机构
[1] Changan Univ, Sch Water & Environm, Xian 710054, Peoples R China
[2] Changan Univ, Key Lab Subsurface Hydrol & Ecol Effect Arid Reg, Minist Educ, Xian 710054, Peoples R China
[3] Changan Univ, Key Lab Ecohydrol & Water Secur Arid, Semiarid Reg Minist Water Resources, Xian 710054, Peoples R China
[4] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
[5] Chongqing Univ, Key Lab Low grade Energy Utilizat Technol & Syst, Minist Educ China, Chongqing 400044, Peoples R China
基金
中国博士后科学基金;
关键词
Supercritical water gasification; Biomass; Thermodynamic analysis; Poly-generation; HYDROGEN-PRODUCTION; PERFORMANCE;
D O I
10.1016/j.energy.2024.133435
中图分类号
O414.1 [热力学];
学科分类号
摘要
Biomass energy is renewable and abundant worldwide, providing a solution for the shortages of fossil fuels and the serious environmental pollution. The proposal for efficient utilization methods of biomass waste demands urgent attention. Supercritical water gasification (SCWG) process is a potential technology. In this work, a polygeneration system based on SCWG was developed to convert biomass waste to gas, biochar, heat, and electricity. Firstly, the mass, energy, and exergy flows were calculated under typical conditions. Subsequently, the impact of various operating parameters on the yield of hydrogen-rich syngas, generated electricity, and the thermodynamic performance of the system was investigated. The results demonstrated that exergy loss primarily occurred in the cooler, reactor, heat exchanger, and preheater, accounting for more than 90 % of the total exergy loss under different conditions. This loss arose from irreversible reactions, heat transfer, and heat dissipation. Higher temperatures, higher biomass concentrations, and greater amounts of preheated water positively affected hydrogen-rich gas production and supplied heat energy. Energy efficiency increased with the rising quantities of preheated water and biomass concentration, with the impact of biomass concentration being more significant. Conversely, the evaluated gasification temperature displayed an adverse effect on energy efficiency. The maximal exergy efficiency reached approximately 58.3 % at 550 degrees C, with a biomass concentration of 33 % and a preheated water mass flow rate of 900 kg h-1.
引用
收藏
页数:12
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