Enhancement effect of semicoke waste heat on energy conservation and hydrogen production from biomass gasification

被引:0
|
作者
Zhang, Junxia [1 ,2 ,3 ]
Zhong, Junfeng [1 ,2 ]
Yang, Li [1 ,2 ]
Wang, Zehua [1 ,2 ,4 ]
Chen, Dongrui [1 ,2 ]
Wang, Qiaoli [1 ,2 ]
机构
[1] Shaoyang Univ, Sch Mech, Shaoyang City 422000, Hunan Province, Peoples R China
[2] Shaoyang Univ, Energy Engn Coll, Shaoyang City 422000, Hunan Province, Peoples R China
[3] Shaoyang Univ, Key Lab Hunan Prov Efficient Power Syst & Intelli, Shaoyang City 422000, Hunan Province, Peoples R China
[4] Haikou Totem New Energy Applicat & Res Dev Co Ltd, Haikou 572000, Hainan Province, Peoples R China
基金
中国国家自然科学基金;
关键词
Waste heat recovery; Biomass gasification; Energy conservation; H-2; CO2; RICH GAS-PRODUCTION; RECOVERY; COKE; MODEL; BED; CO2;
D O I
10.1016/j.renene.2024.121340
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Key approaches to alleviating global warming and curbing fossil fuel depletion involve various industrial energy-conservation technologies and carbon dioxide (CO2) emission reduction methods. The production of hydrogen (H-2)-rich gas from inexpensive and readily available biomass, as an alternative energy source, is becoming increasingly promising. However, this application faces challenges such as high energy consumption and low gas quality. In this study, the waste heat released by semicoke production from lignite gasification and CO2 from exhaust gas were utilized to gasify biomass. This approach aims to save energy in biomass gasification and use CO2 in exhaust gas to improve the H-2 content in biogas. A simulation was conducted to recover semicoke waste heat by combining a suspension tube with CO2 flow to generate steam and high-temperature CO2, which were then simultaneously sent into a gasifier to produce H-2 through biomass gasification. The results revealed that the rate of semicoke waste heat recovery exceeded 90 %. The yield of steam and the rate of waste heat recovery improved with increasing mass flow rate of semicoke and then slightly decreased with increasing steam pressure and CO2 mass flow rate. The yield of H-2 increased with the semicoke mass flow rate and steam pressure. The rate of energy conservation ranged from 15 % to 239 %, peaking at a CO2 mass flow rate of 0.09 kg/s. Compared with the case without waste heat recovery, the economic benefits increased from 12 to 28 times.
引用
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页数:15
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