碳酸钾
碳酸盐
钾
化学
过程(计算)
环境科学
矿物学
环境化学
放射化学
计算机科学
有机化学
操作系统
作者
Kathryn H. Smith,Gongkui Xiao,Kathryn A. Mumford,Jeffri Gouw,Indrawan Indrawan,Navin Thanumurthy,Dimple Mody Quyn,Robyn Cuthbertson,Aravind V. Rayer,Nathan Nicholas,Andrew Lee,Gabe da Silva,Sandra Elizabeth Kentish,Trent Harkin,Abdul Qader,Clare J. Anderson,Barry N. Hooper,Geoffrey Wayne Stevens
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2013-09-17
卷期号:28 (1): 299-306
被引量:90
摘要
A precipitating potassium carbonate (K 2 CO 3 )-based solvent absorption process has been developed by the Cooperative Research Centre for Greenhouse Gas Technologies (CO2CRC) for capturing carbon dioxide (CO 2 ) from industrial sources, such as power plant flue gases. Demonstration of this process is underway using both a laboratory-based pilot plant located at The University of Melbourne and an industrial pilot plant located at the Hazelwood Power Station in Victoria, Australia. The laboratory-scale pilot plant has been designed to capture 4–10 kg/h CO 2 from an air/CO 2 feed gas rate of 30–55 kg/h. The power-station-based pilot plant has been designed to capture up to 1 tonne/day CO 2 from the flue gas of a brown-coal-fired power station. In this paper, results from trials using concentrated potassium carbonate (20–40 wt %) solvent are presented for both pilot plants. Performance data (including pressure drop, holdup, solvent loadings, temperature profile, and CO 2 removal efficiency) have been collected from each plant and presented for a range of operating conditions. Plant data for the laboratory-scale pilot plant (including temperature profiles, solvent loadings, and exit gas CO 2 concentrations) have been used to validate and further develop Aspen Plus simulations, in anticipation of further work involving precipitation and the industry-based pilot plant.
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