Techno-economic analysis of small-scale ammonia production via sorption-enhanced gasification of biomass

被引:12
作者
Dziva, Godknows [1 ,2 ,3 ]
Luan, Chuanbao [1 ]
Ding, Guangchao [2 ]
Bore, Abdoulaye [4 ]
Kouakou, Kouame Jean Ives [1 ]
Tembo, Tinashe [1 ]
Ullah, Atta [5 ]
Zaman, Muhammad [5 ]
Li, Songgeng [2 ,3 ]
Zeng, Liang [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Key Lab Green Chem Technol, Minist Educ, Tianjin 300072, Peoples R China
[2] Chinese Acad Sci, Inst Proc Engn, State Key Lab Mesosci & Engn, Beijing 100190, Peoples R China
[3] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
[4] Tianjin Univ, Sch Environm Sci & Engn, Tianjin Key Lab Biomass Wastes Utilizat, Tianjin 300072, Peoples R China
[5] Pakistan Inst Engn & Appl Sci PIEAS, Dept Chem Engn, Lehtrar Rd, Islamabad 45650, Pakistan
基金
中国国家自然科学基金;
关键词
Steam gasification; Green ammonia; Bioenergy; Carbon capture; Carbon price; STEAM GASIFICATION; CO2; CAPTURE; HYDROGEN; CYCLE; METHANOL; REMOVAL; EXERGY; SYNGAS;
D O I
10.1016/j.cej.2024.151666
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Biomass gasification is a green and efficient pathway for lowering the carbon footprint of ammonia production. Decentralized, small-scale biomass gasification plants (<150 t NH3/day output) are more practical than large plants due to sustainable large-scale biomass supply constraints. Small-scale biomass gasification for ammonia production faces the challenges of high energy consumption and production costs. Process intensification through sorption-enhanced gasification (SEG) integrates steam gasification and in-situ CO2 separation using regenerable CaO sorbents, directly producing hydrogen-rich syngas (similar to 70 vol%), which streamlines syngas conditioning and increases cost-effectiveness. Two SEG process configurations for small-scale biomass-to-ammonia (similar to 45000 t of agricultural residues/year) were proposed: SEG process A, which produced low-carbon ammonia without air separation, and SEG process B, which employed an air separation unit to deliver carbon-negative ammonia by capturing CO2. The two processes were compared against a dual fluidized bed gasification (DFBG) process, which generated green ammonia without an air separation, like SEG process A. Of the three cases, SEG process B showed the lowest biomass (2.14 t biomass/t NH3) and water consumption (0.47 t H2O/t NH3) and avoided 2.8 t CO2/t NH3, making it carbon-negative. While the DFBG process and SEG process A had higher energy efficiencies, SEG process B posted the lowest net energy consumption (36.6 GJ/t NH3). Furthermore, SEG process B had the lowest ammonia production cost ($692/t NH3) and payback time (9.4 years), making it the most economically viable. Sensitivity analysis showed that favorable carbon credit policies could boost the economics of SEG process B to match large-scale plants.
引用
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页数:14
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