Frontiers of Chemical Science and Engineering >
A thermodynamic study of the removal of HCl and H2S from syngas
Received date: 20 Jul 2011
Accepted date: 10 Dec 2011
Published date: 05 Mar 2012
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Advanced integrated-gasification combined-cycle (IGCC) and integrated-gasification fuel cell (IFGC) systems require high-temperature sorbents that are capable of removing hydrogen chloride and hydrogen sulfide from coal derived gases to very low levels. HCl and H2S are highly reactive, corrosive, and toxic gases that must be removed to meet stringent environmental regulations, to protect power generation equipment and to control the emissions of contaminants. The thermodynamic behavior of 13 sorbents for the removal of HCl and H2S under various conditions including: initial toxic gas concentration (1–10000 ppm), operating pressure (0.1–11 Mpa), temperature (300 K–1500 K), and the presence of H2O were investigated. The correlation between HCl and H2S was also examined. Thermodynamic calculations were carried out for the reactions of the 13 sorbents using a FactSage 5.2 software package based on free energy minimization. The sorbents, Na2CO3, NaHCO3, K2CO3, and CaO are capable of completely removing chlorine at high temperatures (up to ~1240 K) and at high pressures. Water vapor did not have any significant effects on the dechlorination capability of the sorbents. Nine of the sorbents namely; Cu2O, Na2CO3, NaHCO3, K2CO3, CaO, ZnO, MnO, FeO, and PbO, were determined to have great potential as desulfurization sorbents. Cu2O and ZnO had the best performance in terms of the optimum operating temperature. The addition of water vapor to the reactant gas produces a slightly detrimental effect on most of the sorbents, but FeO exhibited the worst performance with a reduction in the maximum operating temperature of about 428 K. The dechlorination performance of the alkali sorbents was not affected by the presence of H2S in the reactions. However, the desulfurization capability of some sorbents was greatly affected by the presence of HCl. Particularly, the performance of Cu2O was significantly reduced when HCl was present, but the performance of FeO improved remarkably. The thermodynamic results gathered are valuable for the developments of better sorbents.
Key words: syngas cleaning; sorbent; desulfurization; dechlorination
Joseph LEE , Bo FENG . A thermodynamic study of the removal of HCl and H2S from syngas[J]. Frontiers of Chemical Science and Engineering, 2012 , 6(1) : 67 -83 . DOI: 10.1007/s11705-011-1162-4
1 |
Gasper-Galvin L D, Atimtay A T, Gupta R P. Zeolite-supported metal oxide sorbents for hot-gas desulfurization. Industrial & Engineering Chemistry Research, 1998, 37(10): 4157-4166
|
2 |
Krishnan G, Gupta R.Development of disposable sorbents for chloride removal from high temperature coal-derived gases. DE-AC21-93MC30005-02, 1999
|
3 |
Krishnan G N, Tong G T, Wood B J, Korens N. High-Temperature Coal-Gas Chloride Cleanup for MCFC Applications. DOE/ME/21167-2080, Morgantown Energy Technology Center, US Department of Energy, Morgantown, WV, 1986 Googlescholar
|
4 |
Walters J K, Akosman C. The removal of HCl from hot gases with solid sorbents. In: Schimdt E, Gang P, Pilz T, Dittler A, eds. High Temperature Gas Cleaning. Germany: Instiut fur Mechanischle verfaherstechnik and Mechanik, Karlsuhe, 1996
|
5 |
Newby R A. Base Program Final Report. DE-AC26-99FT40674, 2001
|
6 |
Westmoreland P R, Harrison D P. Evaluation of candidate solids for high-temperature desulfurization of low-Btu gases. Environmental Science & Technology, 1976, 10(7): 659-661
|
7 |
Gupta R, Gangwal S K, Jain S C. Development of zinc ferrite sorbents for desulfurization of hot coal gas in a fluid-bed reactor. Energy & Fuels, 1992, 6(1): 21-27
|
8 |
Atimtay A T, Gasper-Galvin L D, Poston J A. Novel supported sorbent for hot gas desulfurization. Environmental Science & Technology, 1993, 27(7): 1295-1303
|
9 |
Abbasian J, Slimane R B. A regenerable copper-based sorbent for H2S removal from coal gases. Industrial & Engineering Chemistry Research, 1998, 37(7): 2775-2782
|
10 |
Rosenqvist T. Phase equilibria in the pyrometallurgy of sulfide ores. Metallurgical Transactions B, 1978, 9(4): 337-351
|
11 |
Slimane R B, Abbasian J. Copper-based sorbents for coal gas desulfurization at moderate temperatures. Industrial & Engineering Chemistry Research, 2000, 39(5): 1338-1344
|
12 |
Pineda M, Palacios J M, Alonso L, Garcia E, Moliner R. Performance of zinc oxide based sorbents for hot coal gas desulfurization in multicycle tests in a fixed-bed reactor. Fuel, 2000, 79(8): 885-895
|
13 |
Zeng Y, Kaytakoglu S, Harrison D P. Reduced cerium oxide as an efficient and durable high temperature desulfurization sorbent. Chemical Engineering Science, 2000, 55(21): 4893-4900
|
14 |
Akiti T T J, Constant K P, Doraiswamy L K, Wheelock T D. A regenerable calcium-based core-in-shell sorbent for desulfurizing hot coal gas. Industrial & Engineering Chemistry Research, 2002, 41(3): 587-597
|
15 |
Abbasian J, Wangerow J R, Hill A H. Effect of HCl on sulfidation of calcium oxide. Chemical Engineering Science, 1993, 48(15): 2689-2695
|
16 |
Gupta R P, O'Brien W S. Desulfurization of hot syngas containing hydrogen chloride vapors using zinc titanate sorbents. Industrial & Engineering Chemistry Research, 2000, 39(3): 610-619
|
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