DOI QR코드

DOI QR Code

12wt% Co 담지 촉매에서 합성오일 제조시 조촉매 효과 및 반응조건 영향 분석

The Effect of Promotor and Reaction Condition for FT Oil Synthesis over 12wt% Co-based Catalyst

  • 박연희 (한국가스공사 연구개발원) ;
  • 이지윤 (한국가스공사 연구개발원) ;
  • 정종태 (한국가스공사 연구개발원) ;
  • 이종열 (한국가스공사 연구개발원) ;
  • 조원준 (한국가스공사 연구개발원) ;
  • 백영순 (한국가스공사 연구개발원)
  • 투고 : 2014.04.02
  • 심사 : 2014.06.30
  • 발행 : 2014.06.30

초록

The synthesis of Fischer-Tropsch oil is the catalytic hydrogenation of CO to give a range of products, which can be used for the production of high-quality diesel fuel, gasoline and linear chemicals. Our cobalt based catalyst was prepared Co/alumina, silica and titania by the incipient wet impregnation of the nitrates of cobalt and promoter with supports. Cobalt catalysts was calcined at $350^{\circ}C$ before being loaded into the FT reactors. After the reduction of catalyst has been carried out under $450^{\circ}C$ for 24hrs, FT reaction of the catalyst has been carried out at GHSV of 4,000/hr under $200^{\circ}C$ and 20atm. From these test results, we have obtained the results as following ; in case of 12wt% Co-supported $Al_2O_3$, $SiO_2$ and $TiO_2$ catalysts, maximum activities of the catalysts were appeared at the promoters of Mn, Mo and Ce respectively. The activity of 12wt% $Co/Al_2O_3$ added a Mn promoter was about 3 times as high as that of 12wt% $Co/Al_2O_3$ catalyst without promoters. When it has been the experiment at the range of reaction temperature of $200{\sim}220^{\circ}C$ and GHSV of 1,546~5,000/hr, the results have shown generally increasing the activities with the increase of reaction temperature and GHSV.

키워드

참고문헌

  1. Dry, M. E., "ractical and Theoretical Aspects of the Catalytic Fischer-Tropsch Process," Appl. Catal. A-Gen., 1996, Vol. 138, pp. 319-344. https://doi.org/10.1016/0926-860X(95)00306-1
  2. Patzek, T. W. and Croft, G. D., "otential for Coalto-liquids Conversion in the United States: Fischer-Tropsch Synthesis," Nat. Resour. Res., 2009, Vol 18, pp. 181-191. https://doi.org/10.1007/s11053-009-9098-9
  3. Davis, B. H., "ischer-Tropsch synthesis: Overview of Reactor Development and Future Potentialities," Topics in Catalysis, 2005, Vol. 32, pp. 143-168. https://doi.org/10.1007/s11244-005-2886-5
  4. Davis, B. H., "ischer-Tropsch synthesis: Reaction Mechanisms for Iron Catalysts," Catal. Today, 2009, Vol. 141, pp 25-33. https://doi.org/10.1016/j.cattod.2008.03.005
  5. Bian, G., Oonuki, A., Koizumi, N., Nomoto, H. and Yamada, M., "tudies with a Precipitated Iron Fischer-Tropsch Catalyst Reduced by H2 or CO," J. Mol. Catal. A-Chem., 2002, Vol. 186, pp. 203-213. https://doi.org/10.1016/S1381-1169(02)00186-3
  6. T.V. Reshetenko, L.B. Avdeeva, A.A. Khassin, G.N. Kustova, V.A. Ushakov, E.M. Moroz, A.N. Shmakov, V.V. Kriventsov, D.I. Kochubey, Yu.T. Pavlyukhin, A.L. Chuvilin, Z.R. Ismagilov, Appl. Catal. A: Gen., 2004, Vol. 268, pp. 127. https://doi.org/10.1016/j.apcata.2004.03.045
  7. V.A. de la Pena O'Shea, N.N. Menendez, J.D. Tornero, J.L.G. Fierro Catal. Lett., 88 (2003), p. 123. https://doi.org/10.1023/A:1024097319352
  8. D.J. Duvenhage, N.J. Coville, Appl. Catal. A: Gen., 1997, Vol. 153, pp. 43. https://doi.org/10.1016/S0926-860X(96)00326-2
  9. D. Banerjee, D.K. Chakrabarthy, Ind. J. Technol., 1992, Vol. 30, pp. 81.
  10. H. Arai, K. Mitsuishi, T. Seiyama, Chem. Lett. 1984, pp. 1291.
  11. I. Puskas, T.H. Fleisch, J.A. Kaduk, C.L. Marshall, B.L. Meyers, M.J. Castagnola, J.E. Indacochea, Applied Catalysis A: General, 2007, Vol. 316, Issue 2, pp. 197-206. https://doi.org/10.1016/j.apcata.2006.09.029
  12. C.J. Kim, US Patent 0,355,216 (1993).
  13. Snejana Bakardjieva, Jan Subrt, Vaclav Stengl, Maria Jesus Dianez, Maria Jesus Sayagues, Applied Catalysis B: Environmental, 2005, Vol. 58, Issues 3-4, pp. 193-202. https://doi.org/10.1016/j.apcatb.2004.06.019