Experimental Study on the Selective Removal of SO2 from a Ship Exhaust Gas Stream Using a Membrane Contactor

被引:22
作者
Park, Hyung Jin [1 ,3 ]
Bhatti, Umair H. [1 ,2 ]
Joo, Sang Hyun [1 ,3 ]
Nam, Sung Chan [1 ]
Park, Sung Yeol [1 ]
Lee, Ki Bong [3 ]
Baek, Il Hyun [1 ]
机构
[1] Korea Inst Energy Res, Greenhouse Gas Lab, Daejeon 34129, South Korea
[2] Univ Sci & Technol, Daejeon 34113, South Korea
[3] Korea Univ, Dept Chem & Biol Engn, Seoul, South Korea
关键词
MASS-TRANSFER; CARBON-DIOXIDE; FLUE-GAS; CO2; SEPARATION; PACKED TOWER; NITRIC-OXIDE; ABSORPTION; PERFORMANCE; CAPTURE; H2S;
D O I
10.1021/acs.iecr.9b01181
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, we investigated the selective SO2 removal performance of three absorbents-distilled water (DW), aqueous NaOH, and Na(2)SO(3 )solutions-from a typical ship exhaust gas stream using a hollow-fiber membrane contactor. SEM and contact angle analyses were performed to apprehend the morphological and water interaction characteristics of the membrane. A SO2/CO2/N-2 gas mixture (1000 ppm of SO2, 5.50 mol % CO2, balance N-2) was used and the absorbents were thoroughly evaluated in terms of SO2 gas removal efficiency over a range of operating parameters including absorbent flow rate, feed gas flow rate, absorbent concentration, and L/G ratio. The aq. NaOH absorbent had the best SO2 removal efficiency among the three absorbents under all conditions, mainly due to high alkalinity. Notably, around 100% SO2 removal efficiency can be achieved with the NaOH absorbent. The Na2SO3 solution closely followed the NaOH in SO2 removal efficiency. DW was the worst performer under all conditions. This study confirms that the use of membrane contactor is advantageous over the conventional packed towers because the membrane contactors are compact, offer high contact area, and achieve higher removal efficiencies.
引用
收藏
页码:14897 / 14905
页数:9
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