Articles & Issues
- Language
- korean
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received September 1, 2011
Accepted September 22, 2011
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.
All issues
수열특성 및 기계적 안정성의 개선으로 슬러리상 CSTR에 적합한 P 첨가 알루미나 기반의 Fischer-Tropsch 합성용 코발트 촉매
Phosphorus Modified Co/Al2O3 Fischer-Tropsch Catalyst for a Slurry Phase CSTR with Enhanced Hydrothermal and Mechanical Stability
Gyu-In Jung1 2
Kyoung-Su Ha1†
Seon-Ju Park1
Du-Eil Kim1
Min-Hee Woo1
Ki-Won Jun1
Jong-Wook Bae3
Yong Kang2†
1한국화학연구원 그린화학촉매연구센터, 305-600 대전광역시 유성구 신성로 19 2충남대학교 화학공학과, 305-764 대전시 유성구 궁동 220 3성균관대학교 화학공학과, 440-746, 경기도 수원시 장안구 천천동 300
1Research Center for Green Catalysis, Korea Research Institute of Chemical Technology, 19 Sinseong-ro, Yuseong-gu, Daejeon 305-600, Korea 2School of Chemical Engineering, Chungnam National University, 220 Gung-dong, Yuseong-gu, Daejeon 305-764, Korea 3Department of Chemical Engineering, Sungkyunkwan University, 300 Chunchun-dong, Jangan-gu, Suwon-si, Gyeonggi-do 440-746, Korea
filoseus@krict.re.kr
Korean Chemical Engineering Research, April 2012, 50(2), 229-237(9), NONE Epub 30 March 2012
Download PDF
Abstract
Fischer-Tropsch 합성용 Co/Al2O3 촉매에서 알루미나 지지체에 인산 용액으로 알루미나 표면을 개질하여 촉매적 활성은 물론이고, 기계적 강도와 수열 안정성을 개선하였다. FT-IR과 같은 촉매 표면 분석법을 통하여 P 첨가로 알루미나 표면에 AlPO4 상이 생성되어 촉매인 코발트와 지지체인 알루미나 사이의 상호작용이 약화되어 촉매의 환원도가 높아졌음을 보였다. 이에 따른 촉매성능을 평가하기 위하여 C5+ productivity와 turnover frequency를 계산하였다. 또한, 2 wt.%P 첨가 알루미나를 대상으로 지지체의 소성온도가 촉매활성에 미치는 영향도 살펴보았다. 한편, 고온 가압 하에서 물을 이용하여 P 첨가 알루미나(P-알루미나)를 지지체로 한 촉매의 수열 특성을 살펴보았으며, 실험 전후의 XRD 패턴을 분석함으로써 P 첨가 알루미나 기반 촉매가 수열 안정성이 우수하다는 것을 증명하였다. 뿐만 아니라, 촉매의 기계적 강도를 측정하기 위하여 유동화 반응기를 직접 제작하여 P-알루미나 기반 촉매의 P 함량이 증가할수록 마모도가 감소함을 확인하였다. 촉매 활성, 수열 안정성, 그리고 기계적 강도를 모두 고려하면, 알루미나에 첨가된 P의 함량이 1~2 wt.% 이고, 지지체를 500 ℃에서 소성하여 제조한 촉매가 가장 좋은 성능을 보였다.
Phosphorus was incorporated into Co/Al2O3 catalyst for FTS by impregnating an acidic precursor, phosphoric acid, in γ-Al2O3 support to improve the mechanical strength, the hydrothermal stability of the catalyst particle, and the catalytic performance as well. Surface characterization techniques such as FT-IR revealed that AlPO4 phase was generated on the surface of the P-modified catalyst. The addition of phosphorus was found to alleviate the interaction between cobalt and alumina surface, and to increase reducibility of catalyst. The catalytic activity such as C5+ productivity and turnover frequency (TOF) was calculated to evaluate catalytic performance. The influence of calcination temperature of the Al2O3 containing 2 wt.% P on the catalytic performance was also investigated. Through hydrothermal stability test and XRD analysis, the P-modified catalyst had strong resistant to the pressurized and hot H2O. The mechanical strength of the P-modified catalyst was also examined through an in-house fluidized-bed vessel, and it was found that the catalyst fragmentation could be successfully suppressed with P. Taken as a whole, the best performance was shown to be at 1~2 wt.% P in alumina and at the calcination temperature of 500 ℃.
References
Khodakov AY, Chu W, Fongarland P, Chem. Rev., 107(5), 1692 (2007)
Dry ME, Catal. Today, 71(3-4), 227 (2002)
Ha KS, Bae JW, Woo KJ, Jun KW, Environ. Sci. Technol., 44, 1412 (2010)
Bae JW, Kim SM, Lee YJ, Lee MJ, Jun KW, Catal. Commun., 10, 1358 (2009)
Morterra C, Magnacca G, Demaestri PP, J. Catal., 152(2), 384 (1995)
Iwamoto R, Grimblot J, Adv. Catal., 44, 417 (1999)
Zhao R, Goodwin JG, Oukaci R, Appl. Catal. A: Gen., 189(1), 99 (1999)
Park SJ, Bae JW, Oh JH, Chary KVR, Prasad PSS, Jun KW, Rhee YW, J. Mol. Catal. A-Chem., 298(1-2), 81 (2009)
Quartararo J, Guelton M, Rigole M, Amoureux JP, Fernandez C, Grimblot J, J. Mater Chem.,, 9, 2637 (1999)
Chary KVR, Kishan G, Ramesh K, Kumar CP, Vidyasagar G, Langmuir, 19(11), 4548 (2003)
Bautista FM, Campelo JM, Garcia A, Luna D, Marinas JM, Romero AA, Colon G, Navio JA, Macias M, J. Catal., 179(2), 483 (1998)
Schanke D, Vada S, Blekkan EA, Hilmen AM, Hoff A, Holmen A, J. Catal., 156(1), 85 (1995)
Bezemer GL, Bitter JH, Kuipers HPCE, Oosterbeek H, Holewijn JE, Xu XD, Kapteijn F, van Dillen AJ, de Jong KP, J. Am. Chem. Soc., 128(12), 3956 (2006)
Oukaci R, “F-T Synthesis Process,” XTL Fundamentals, December, Cape Town, South Africa (2009)
Patterson AL, Phys. Rev., 56, 978 (1939)
Dry ME, Catal. Today, 71(3-4), 227 (2002)
Ha KS, Bae JW, Woo KJ, Jun KW, Environ. Sci. Technol., 44, 1412 (2010)
Bae JW, Kim SM, Lee YJ, Lee MJ, Jun KW, Catal. Commun., 10, 1358 (2009)
Morterra C, Magnacca G, Demaestri PP, J. Catal., 152(2), 384 (1995)
Iwamoto R, Grimblot J, Adv. Catal., 44, 417 (1999)
Zhao R, Goodwin JG, Oukaci R, Appl. Catal. A: Gen., 189(1), 99 (1999)
Park SJ, Bae JW, Oh JH, Chary KVR, Prasad PSS, Jun KW, Rhee YW, J. Mol. Catal. A-Chem., 298(1-2), 81 (2009)
Quartararo J, Guelton M, Rigole M, Amoureux JP, Fernandez C, Grimblot J, J. Mater Chem.,, 9, 2637 (1999)
Chary KVR, Kishan G, Ramesh K, Kumar CP, Vidyasagar G, Langmuir, 19(11), 4548 (2003)
Bautista FM, Campelo JM, Garcia A, Luna D, Marinas JM, Romero AA, Colon G, Navio JA, Macias M, J. Catal., 179(2), 483 (1998)
Schanke D, Vada S, Blekkan EA, Hilmen AM, Hoff A, Holmen A, J. Catal., 156(1), 85 (1995)
Bezemer GL, Bitter JH, Kuipers HPCE, Oosterbeek H, Holewijn JE, Xu XD, Kapteijn F, van Dillen AJ, de Jong KP, J. Am. Chem. Soc., 128(12), 3956 (2006)
Oukaci R, “F-T Synthesis Process,” XTL Fundamentals, December, Cape Town, South Africa (2009)
Patterson AL, Phys. Rev., 56, 978 (1939)