Kinetic study of propane dehydrogenation and catalyst deactivation over Pt-Sn/Al2O3 catalyst

被引:33
作者
Zangeneh, Farnaz Tahriri [1 ]
Taeb, Abbas [1 ]
Gholivand, Khodayar [1 ]
Sahebdelfar, Saeed [2 ]
机构
[1] Islamic Azad Univ, Dept Chem, Sci & Res Branch, Tehran, Iran
[2] Natl Petrochem Co, Petrochem Res & Technol Co, Catalyst Res Grp, Tehran, Iran
关键词
propane dehydrogenation; Pt-Sn/Al2O3; kinetics; catalyst deactivation; mass transfer limitation; PERFORMANCE; ISOBUTANE; PARAFFINS; HYDROGEN; OLEFINS; REACTOR; STEAM; TIN; SN;
D O I
10.1016/S2095-4956(13)60096-0
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The kinetics of propane dehydrogenation and catalyst deactivation over Pt-Sn/Al2O3 catalyst were studied. Performance test runs were carried out in a fixed-bed integral reactor. Using a power-law rate expression for the surface reaction kinetics and independent law for deactivation kinetics, the experimental data were analyzed both by integral and a novel differential method of analysis and the results were compared. To avoid fluctuation of time-derivatives of conversion required for differential analysis, the conversion-time data were first fitted with appropriate functions. While the time-zero and rate constant of reaction were largely insensitive to the function employed, the rate constant of deactivation was much more sensitive to the function form. The advantage of the proposed differential method, however, is that the integration of the rate expression is not necessary which otherwise could be complicated or impossible. It was also found that the reaction is not limited by external and internal mass transfer limitations, implying that the employed kinetics could be considered as intrinsic ones.
引用
收藏
页码:726 / 732
页数:7
相关论文
共 23 条
[1]   Propane dehydrogenation activity of Pt and Pt-Sn catalysts supported on magnesium aluminate:: influence of steam and hydrogen [J].
Aguilar-Ríos, G ;
Salas, P ;
Valenzuela, MA ;
Armendáriz, H ;
Wang, JA ;
Salmones, J .
CATALYSIS LETTERS, 1999, 60 (1-2) :21-25
[2]  
[Anonymous], 2005, TRANSPORT PHENOMENA
[3]   Kinetics for dehydrogenation of propane on Pt-Sn-K/γ-Al2O3 catalyst [J].
Assabumrungrat, S ;
Jhoraleecharnchai, W ;
Praserthdam, P ;
Goto, S .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2000, 33 (03) :529-532
[4]   Dehydrogenation and oxydehydrogenation of paraffins to olefins [J].
Bhasin, MM ;
McCain, JH ;
Vora, BV ;
Imai, T ;
Pujadó, PR .
APPLIED CATALYSIS A-GENERAL, 2001, 221 (1-2) :397-419
[5]   Modeling of a radial-flow moving-bed reactor for dehydrogenation of isobutane [J].
Bijani, Parisa Moghimpour ;
Sahebdelfar, Saeed .
KINETICS AND CATALYSIS, 2008, 49 (04) :599-605
[6]  
Ertl C, 1997, HDB HETEROGENEOUS CA, V4, P2140
[7]  
Fogler H., 2006, Elements of Chemical Reaction Engineering, V5th, P757
[8]  
Heinritz-Adrian M., 2008, PETROLEUM TECHNOLOGY, V13, P83
[9]   Dehydrogenation of propane on modified Pt/θ-alumina Performance in hydrogen and steam environment [J].
Kogan, SB ;
Schramm, H ;
Herskowitz, M .
APPLIED CATALYSIS A-GENERAL, 2001, 208 (1-2) :185-191
[10]  
Le Page J F, 1987, APPL HETEROGENEOUS C, P41