New environmentally attractive separation technology for flue gas mixture

被引:2
作者
Animasahun, Olamide H. [1 ]
Khan, Muhammad N. [1 ]
Peters, Cornelis J. [1 ,2 ]
机构
[1] Khalifa Univ Sci & Technol, Dept Chem Engn, Petr Inst, POB 2533, Abu Dhabi, U Arab Emirates
[2] Colorado Sch Mines, Dept Chem Engn, Golden, CO 80401 USA
关键词
Gas separation; hydrates; carbon dioxide; equations of state; HEAT-EXCHANGER NETWORKS; CARBON-DIOXIDE CAPTURE; PRESSURE RECOVERY; CO2; CAPTURE; HYDRATE; GENERATION; ENERGY;
D O I
10.1080/00268976.2018.1509145
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Separation of gaseous mixtures produced from any process plant can be a major issue for the industry. In comparison to other separation techniques available, hydrate formation can be an appropriate choice in terms of fuel efficiency and degree of separation. In this work, a three- stage process was designed to capture CO2 from a hypothetical flue gas mixture ( comprising 15 mol% CO2 + 85 mol% N2). For the hydrate based CO2 capture process, a detailed analysis was carried out covering the material and energy balance, energy integration and economic analysis. The results show that, at steady state, 91% of the CO2 in the flue gas can be recovered, resulting into two streams: Stream- A ( 94 mol% CO2 + 6 mol% N2) and Stream- B ( 1.5 mol% CO2 + 98.5 mol% N2). Per 100 mol of the flue gas feed, 3.9MW of energy is required to achieve such degree of separation. This amount was reduced to 2.4MWafter energy integration was applied to the process. Overall, the process can help in reducing CO2 emission via flue gas because of the huge difference in the carbon foot print of its energy requirement ( 500 g CO2 per kWh) and the amount of CO2 captured by the process ( 2190 g CO2 per kWh). [GRAPHICS]
引用
收藏
页码:3434 / 3445
页数:12
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