Kinetics for dehydrogenation of propane on Pt-Sn-K/γ-Al2O3 catalyst

被引:13
作者
Assabumrungrat, S [1 ]
Jhoraleecharnchai, W
Praserthdam, P
Goto, S
机构
[1] Chulalongkorn Univ, Dept Chem Engn, Petrochem Engn Lab, Bangkok 10330, Thailand
[2] Nagoya Univ, Dept Chem Engn, Nagoya, Aichi 4648603, Japan
关键词
dehydrogenation; propane; propene; kinetics; platinum-based catalyst;
D O I
10.1252/jcej.33.529
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The performance of three catalysts, namely Pt/gamma-Al2O3, Pt-Sn/gamma-Al2O3 and Pt-Sn-K/gamma-Al2O3 for dehydrogenation of propane is discussed. All catalysts are found to be highly selective towards propene. PtSn-K/gamma-Al2O3 appears to be the most stable and suitable catalyst for the dehydrogenation of propane. PtSn/gamma-Al2O3 is also found to be superior to Pt/gamma-Al2O3. In the kinetic study, the reaction rate constants based on the number of active sites are calcnlated from the apparent reaction rate constants and the number of metal active sites. The reaction rate constants for Pt/gamma-Al2O3, Pt-Sn/gamma-Al2O3 and Pt-Sn-K/gamma-Al2O3 catalysts at 773 K are 0.48 x 10(-28), 0.67 x 10(-28) and 2.98 x 10(-28) moll(site.s.Pa), respectively, In addition, for Pt-Sn-K/gamma-Al2O3, the frequency factor and the activation energy are 6.14 x 10(-24) mol/(site.s.Pa) and 62.7 kJ/mol, respectively.
引用
收藏
页码:529 / 532
页数:4
相关论文
共 11 条
[1]   PROPANE DEHYDROGENATION OVER SUPPORTED PLATINUM CATALYSTS - EFFECT OF TIN AS A PROMOTER [J].
BARIAS, OA ;
HOLMEN, A ;
BLEKKAN, EA .
CATALYSIS TODAY, 1995, 24 (03) :361-364
[2]   Propane dehydrogenation over supported Pt and Pt-Sn catalysts: Catalyst preparation, characterization, and activity measurements [J].
Barias, OA ;
Holmen, A ;
Blekkan, EA .
JOURNAL OF CATALYSIS, 1996, 158 (01) :1-12
[3]   MECHANISM OF THE SELECTIVE REDUCTION OF NITROGEN MONOXIDE ON PLATINUM-BASED CATALYSTS IN THE PRESENCE OF EXCESS OXYGEN [J].
BURCH, R ;
MILLINGTON, PJ ;
WALKER, AP .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1994, 4 (01) :65-94
[4]   EFFECT OF THE ADDITION OF ALKALI-METALS ON THE METALLIC PHASE OF PT/AL2O3 CATALYSTS [J].
DEMIGUEL, SR ;
CASTRO, AA ;
SCELZA, OA ;
SORIA, J .
CATALYSIS LETTERS, 1995, 32 (3-4) :281-291
[5]  
Krishnamurthy KR, 1998, STUD SURF SCI CATAL, V113, P139
[6]  
LARRSON M, 1998, APP CAT A, V166, P9
[7]  
LARRSON M, 1997, CATALYST DEACTIVATIO, V111, P673
[8]  
Praserthdam P, 1997, STUD SURF SCI CATAL, V111, P153
[9]   Observations, modeling and optimization of yield, selectivity and activity during dehydrogenation of isobutane and propane in a Pd membrane reactor [J].
Sheintuch, M ;
Dessau, RM .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (04) :535-547
[10]   Dehydrogenation of propane using a packed-bed catalytic membrane reactor [J].
Weyten, H ;
Keizer, K ;
Kinoo, A ;
Luyten, J ;
Leysen, R .
AICHE JOURNAL, 1997, 43 (07) :1819-1827