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CO2 capture from hot stove gas in steel making process
Authors:Hsu-Hsiang Cheng  Jui-Fu Shen  Chung-Sung Tan
Institution:1. Department of Chemical Engineering, National Tsing Hua University, Hsinchu 30013, Taiwan, ROC;2. New Material Research & Development Department, China Steel Corp., Kaohsiung 81233, Taiwan, ROC;1. DIME sez.MASET, University of Genova, Via Montallegro 1, 16145 Genova, Italy;2. School of Engineering, University of Hull, Hull HU6 7RX, UK;1. Gas Processing Centre, College of Engineering, Qatar University, Doha, Qatar;2. Åbo Akademi University, Thermal and Flow Engineering, Turku, Finland;3. Department of Chemical Engineering, College of Engineering, Qatar University, Doha, Qatar;1. VTT Technical Research Centre of Finland, P.O. Box 1603, FI-40101 Jyväskylä, Finland;2. Ruukki Metals Oy, Rautaruukintie 155, 92100 Raahe, Finland
Abstract:The capture of CO2 from a hot stove gas in steel making process containing 30 vol% CO2 by chemical absorption in a rotating packed bed (RPB) was studied. The RPB had an inner diameter of 7.6 cm, an outer diameter of 16 cm, and a height of 2 cm. The aqueous solutions containing 30 wt% of single and mixed monoethanolamine (MEA), 2-(2-aminoethylamino)ethanol (AEEA), and piperazine (PZ) were used. The CO2 capture efficiency was found to increase with increasing temperature in a range of 303–333 K. It was also found to be more dependent on gas and liquid flow rates but less dependent on rotating speed when the speed was higher than 700 rpm. The obtained results indicated that the mixed alkanolamine solutions containing PZ were more effective than the single alkanolamine solutions. This was attributed to the highest reaction rate of PZ with CO2. A higher portion of PZ in the mixture was more favorable to CO2 capture. The highest gas flow rates allowed to achieve a desired CO2 capture efficiency and the correspondent height of transfer unit (HTU) were determined at different aqueous solution flow rates. Because all the 30 wt% single and mixed alkanolamine solutions could result in a HTU less than 5.0 cm at a liquid flow rate of 100 mL/min, chemical absorption in a RPB instead of a packed bed adsorber is therefore suggested to capture CO2 from the flue gases in steel making processes.
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