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Conference Paper: Reuse of an aerobically treated wastewater effluent for the removal of SO2 in the flue gas
Title | Reuse of an aerobically treated wastewater effluent for the removal of SO2 in the flue gas |
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Authors | |
Keywords | Absorption desulfurization flue gas reuse SO2 wastewater |
Issue Date | 2003 |
Publisher | IWA Publishing. |
Citation | The 3rd World Water Congress of the International Water Association, Melbourne, Australia, 7-12 April 2002. In Water Science & Technology, 2003, v. 3 n. 3, p. 101-107 How to Cite? |
Abstract | Aerobically treated wastewater effluent (ATWE), intrinsically having high alkalinity, was used to remove sulfur dioxide (SO2) in the flue gas of a coal power plant. Experimental results conducted in a four sieve-tray tower showed that ATWE absorbed SO2 in flue gas effectively. At a gas:liquid (G:L) ratio of 110:1, the respective SO2 removal efficiencies were 99% and 95% for flue gases containing 1,600 and 5,000 Mg/kL of SO2. When the G:L ratio increased to 220:1, the removal efficiency was slightly lowered to 93% for the flue gas containing 1,600 Mg/kL of SO2. ATWE had higher buffer capacity and SO2 removal efficiencies as compared to seawater, a common SO2 scrubbing medium serving as control. In addition, the equilibrium equation between SO2 partial pressure and concentration of bisulfite (HSO3-) in ATWE and the kinetic equation describing the rate of SO2 absorption in the sieve-tray tower by ATWE were established. The absorbing coefficients in the kinetic equation were determined to be 1.96 ± 0.37 mol/(m2ásábar) for gas phase and 0.00184 ± 0.00049 m/s for liquid film. The enhancement factor of the absorbing coefficient in liquid film was 14.28 ± 1.79, resulting in 93% of the decrease of liquid film resistance. The SO2 absorption rate in the sieve-tray tower was mainly affected by the gas film resistance, representing 96% of the total resistance. Experimental results of this study confirmed that the removal of SO2 from the flue gas of coal power plants by ATWE was cost-effective. This process does not require the addition of any chemicals and produces no secondary pollution. |
Persistent Identifier | http://hdl.handle.net/10722/111100 |
ISSN | 2023 Impact Factor: 1.9 2023 SCImago Journal Rankings: 0.452 |
DC Field | Value | Language |
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dc.contributor.author | Liu, Y | en_HK |
dc.contributor.author | Ma, LM | en_HK |
dc.contributor.author | Fang, HHP | en_HK |
dc.contributor.author | Gao, TY | en_HK |
dc.contributor.author | Xu, ZX | en_HK |
dc.contributor.author | Wang, YC | - |
dc.contributor.author | Jing, ZG | - |
dc.date.accessioned | 2010-09-26T02:34:33Z | - |
dc.date.available | 2010-09-26T02:34:33Z | - |
dc.date.issued | 2003 | en_HK |
dc.identifier.citation | The 3rd World Water Congress of the International Water Association, Melbourne, Australia, 7-12 April 2002. In Water Science & Technology, 2003, v. 3 n. 3, p. 101-107 | - |
dc.identifier.issn | 1606-9749 | - |
dc.identifier.uri | http://hdl.handle.net/10722/111100 | - |
dc.description.abstract | Aerobically treated wastewater effluent (ATWE), intrinsically having high alkalinity, was used to remove sulfur dioxide (SO2) in the flue gas of a coal power plant. Experimental results conducted in a four sieve-tray tower showed that ATWE absorbed SO2 in flue gas effectively. At a gas:liquid (G:L) ratio of 110:1, the respective SO2 removal efficiencies were 99% and 95% for flue gases containing 1,600 and 5,000 Mg/kL of SO2. When the G:L ratio increased to 220:1, the removal efficiency was slightly lowered to 93% for the flue gas containing 1,600 Mg/kL of SO2. ATWE had higher buffer capacity and SO2 removal efficiencies as compared to seawater, a common SO2 scrubbing medium serving as control. In addition, the equilibrium equation between SO2 partial pressure and concentration of bisulfite (HSO3-) in ATWE and the kinetic equation describing the rate of SO2 absorption in the sieve-tray tower by ATWE were established. The absorbing coefficients in the kinetic equation were determined to be 1.96 ± 0.37 mol/(m2ásábar) for gas phase and 0.00184 ± 0.00049 m/s for liquid film. The enhancement factor of the absorbing coefficient in liquid film was 14.28 ± 1.79, resulting in 93% of the decrease of liquid film resistance. The SO2 absorption rate in the sieve-tray tower was mainly affected by the gas film resistance, representing 96% of the total resistance. Experimental results of this study confirmed that the removal of SO2 from the flue gas of coal power plants by ATWE was cost-effective. This process does not require the addition of any chemicals and produces no secondary pollution. | - |
dc.language | eng | en_HK |
dc.publisher | IWA Publishing. | - |
dc.relation.ispartof | Water Science & Technology | en_HK |
dc.subject | Absorption | - |
dc.subject | desulfurization | - |
dc.subject | flue gas | - |
dc.subject | reuse | - |
dc.subject | SO2 | - |
dc.subject | wastewater | - |
dc.title | Reuse of an aerobically treated wastewater effluent for the removal of SO2 in the flue gas | en_HK |
dc.type | Conference_Paper | en_HK |
dc.identifier.email | Fang, HHP: hrechef@hkucc.hku.hk | en_HK |
dc.identifier.authority | Fang, HHP=rp00115 | en_HK |
dc.identifier.hkuros | 67265 | en_HK |
dc.identifier.issnl | 1606-9749 | - |