Continuous Operation of Zinc-Titanate Sorbent for 100 Hours in a Fluidized Hot Gas Desulfurization Process for IGCC

IGCC용 유동층 고온건식탈황공정에서 Zinc-Titanate 탈황제의 100시간 연속운전 성능실험

Yi, Chang-Keun;Cho, Sung-Ho;Kwon, Hak-Sun;Kim, Keum-Bum;Chae, Hyun-Kue;Jin, Gyoung-Tae;Son, Jae-Ek
이창근;조성호;권학선;김근범;채현규;진경태;손재익

  • Published : 2002.04.30

Abstract

Continuous operation was performed at high pressure and high temperature to see the long-term reactivity and the attrition resistance of the sorbent, the reliability of the process in a bench-scale KIER fluidized hot gas desulfurization process. A spray dried sorbent consisting of zinc-oxide and titanium oxide was used. The pressure was maintained at 5 atm, the temperatures were $600^{\circ}C$ in a desulfurizer and $700^{\circ}C$ in the the regenerator. Solids were circulated continuously and stably between two fluidized reactors at high pressure. The $H_{2}S$ concentration at exit was consistently maintained for 100 hours below 40 ppmv for a simulated coal gas containing 7,700 ppm $H_{2}S$. The analysis of solid samples, such as densities, sulfur content, SEM, Mercury pore analysis, BET, size distribution, were contributed to uncover the characteristics of reactions and entrainment in two fluidized bed reactors.

벤치규모의 고온건식탈황 유동층공정의 연속운전을 탈황제의 장기 반응성, 내마모성, 공정의 신뢰성을 확보하기 위하여 수행하였다. 분무건조법에 의하여 제조된 zinc-titanate 탈황제를 사용하였으며, 반응기 압력은 5기압, 황화반응온도 $600^{\circ}C$, 재생반응온도 $700^{\circ}C$로 유지하였고, 두 유동층 반응기 사이의 탈황제의 고체순환은 안정적이었다. 환원성 연료 가스중에 7,700 ppm의 $H_{2}S$가 황화반응기를 통과한 후 가스중의 황화합물 배출농도를 100시간동안 40 ppm미만으로 연속적으로 유지하였다. 두 유동층 반응기에서의 반응과 비산유출 특성을 밝히기 위하여 입자의 밀도, 황성분, SEM, 수은기공분석, BET, 입도분포 등의 분석이 이루어졌다.

Keywords

References

  1. High Temperature Gas Cleaning Cicero, D.C.;Gupta, R.P.;Turk, B.S.;Portzer, J.W.;Gangwal, S.K.;Dittler, A.(ed.);Hemmer, G.(ed.);Kasper, G.(ed.)
  2. Proc. of the Advanced Coal-Fired Power Systems '95 Review Meeting v.1 Ghazanfari, R.;Feher, G.;Konttinen, J.;Lehtovaara, A.;Mojtahedi, W.
  3. J. of the Japan Institute of Energy v.75 Nakayama, T.;Araki, S.;Takahata, E.;Takahashi, A. https://doi.org/10.3775/jie.75.351
  4. Chemical Industry & Technology v.13 Yi, C.K.;Wi, Y.H.
  5. Chemical Industry and Technology v.15 Rhee, Y.W.;Lee, T.J.;Yi, C.K.
  6. Industrial & Engineering Chemistry Research v.36 no.1 Cu−Cr−O and Cu−Ce−O Regenerable Oxide Sorbents for Hot Gas Desulfurization Li, Z.;Flytzani-Stephanopoulos, M. https://doi.org/10.1021/ie960245d
  7. HWAHAK KONGHAK v.38 Lim, C.J.;Cha, Y.K.;Park, N.K.;Ryu, S.O.;Lee, T.J.;Kim, J.C.
  8. Industrial & Engineering Chemistry Research v.37 no.7 A Regenerable Copper-Based Sorbent for H2S Removal from Coal Gases Abbasian, J.;Slimane, R.B. https://doi.org/10.1021/ie980047h
  9. Fuel Processing Technology v.62 no.1 Characterization of Mn and Cu oxides as regenerable sorbents for hot coal gas desulfurization Alonso, L.;Palacios, J.M.;Garcia, E.;Moliner, R. https://doi.org/10.1016/S0378-3820(99)00063-6
  10. Korean Journal of Chemical Engineering v.14 no.6 A Study on Regeneration of Zinc Titanate Sorbents for H2S Removal Lee, T.J.;Won, W.T.;Chang, W.C.;Kim, J.C. https://doi.org/10.1007/BF02706602
  11. Korean Journal of Chemical Engineering v.17 Reactivity of Copper Oxide-Based Sorbent in Coal Gas Desulfurization Song, Y.K.;Lee, K.B.;Lee, H.S.;Rhee, Y.W. https://doi.org/10.1007/BF02699119
  12. HWAHAK KONGHAK v.37 Yi, C.K.;Park, J.;Cho, S.H.;Jin, G.T.;Son, J.E.
  13. HWAHAK KONGHAK v.39 Yi, C.K.;Cho, S.H.;Son, J.E.;Moon, Y.S.;Choi, J.H.
  14. Enhanced Durability of Desulfurization Sorbents for Fluidized-Bed Applications, DOE Report, DOE/MC/25006-3271 Gupta, R.P.;Gangwal, S.K.
  15. High-Temperature High Pressure Testing of Zinc Titanate in a Bench-Scale Fluidized-Bed Reactor for 100 Cycles, DOE Report, DOE/MC/25006-3492 Gupta, R.P.;Gangwal, S.K.
  16. Korean J. Chem. Eng. v.18 Yi, C.K.;Jo, S.H.;Lee, B.H.;Lee, S.Y.;Son, J.E.;Jin, G.T.
  17. Fluidization Engineering Kunni, D.;Levenspiel, O.