Propane dehydrogenation and coke formation on chromia-alumina catalysts: effect of reductive pretreatments

1992 ◽  
Vol 31 (12) ◽  
pp. 2670-2674 ◽  
Author(s):  
Osvaldo F. Gorriz ◽  
Vicente Cortes Corberan ◽  
Jose L. G. Fierro

Author(s):  
Lohit Sharma ◽  
Stephen C. Purdy ◽  
Katharine Page ◽  
Srinivas Rangarajan ◽  
Hien Pham ◽  
...  


ACS Catalysis ◽  
2020 ◽  
Vol 10 (9) ◽  
pp. 5208-5216 ◽  
Author(s):  
Mostafa Aly ◽  
Esteban L. Fornero ◽  
Andres R. Leon-Garzon ◽  
Vladimir V. Galvita ◽  
Mark Saeys


2011 ◽  
Vol 54 (13-15) ◽  
pp. 888-896 ◽  
Author(s):  
Qing Li ◽  
Zhijun Sui ◽  
Xinggui Zhou ◽  
Yian Zhu ◽  
Jinghong Zhou ◽  
...  


ChemInform ◽  
2010 ◽  
Vol 25 (44) ◽  
pp. no-no
Author(s):  
S. DE ROSSI ◽  
G. FERRARIS ◽  
S. FREMIOTTI ◽  
E. GARRONE ◽  
G. GHIOTTI ◽  
...  


Catalysts ◽  
2020 ◽  
Vol 11 (1) ◽  
pp. 25
Author(s):  
Su-Un Lee ◽  
You-Jin Lee ◽  
Soo-Jin Kwon ◽  
Jeong-Rang Kim ◽  
Soon-Yong Jeong

With the growing global propylene demand, propane dehydrogenation (PDH) has attracted great attention for on-purpose propylene production. However, its industrial application is limited because catalysts suffer from rapid deactivation due to coke deposition and metal catalyst sintering. To enhance metal catalyst dispersion and coke resistance, Pt-based catalysts have been widely investigated with various porous supports. In particular, zeolite can benefit from large surface area and acid sites, which favors high metal dispersion and promoting catalytic activity. In this work, we investigated the PDH catalytic properties of Beta zeolites as a support for Pt-Sn based catalysts. In comparison with Pt-Sn supported over θ-Al2O3 and amorphous silica (Q6), Beta zeolite-supported Pt-Sn catalysts exhibited a different reaction trend, achieving the best propylene selectivity after a proper period of reaction time. The different PDH catalytic behavior over Beta zeolite-supported Pt-Sn catalysts has been attributed to their physicochemical properties and reaction mechanism. Although Pt-Sn catalyst supported over Beta zeolite with low acidity showed low Pt dispersion, it formed a relatively lower amount of coke on PDH reaction and maintained a high surface area and active Pt surfaces, resulting in enhanced stability for PDH reaction. This work can provide a better understanding of zeolite-supported Pt-Sn catalysts to improve PDH catalytic activity with high selectivity and low coke formation.





2018 ◽  
Vol 57 (26) ◽  
pp. 8647-8654 ◽  
Author(s):  
Hai-Zhi Wang ◽  
Li-Li Sun ◽  
Zhi-Jun Sui ◽  
Yi-An Zhu ◽  
Guang-Hua Ye ◽  
...  


2017 ◽  
Vol 42 (4) ◽  
pp. 344-360
Author(s):  
Milad Komasi ◽  
Shohreh Fatemi ◽  
Seyed Hesam Mousavi

Pt–Sn/hierarchical SAPO-34 was synthesised and kinetically modelled as an efficient and selective catalyst for propylene production through propane dehydrogenation. The kinetics of the reaction network were studied in an integral fixed-bed reactor at three temperatures of 550, 600 and 650 °C and weight hourly space velocities of 4 and 8 h−1 with a feed containing hydrogen and propane with relative molar ratios of 0.2, 0.5 and 0.8, at normal pressure. The experiments were performed in accordance with the full factorial experimental design. The kinetic models were constructed on the basis of different mechanisms and various deactivation models. The kinetics and deactivation parameters were simultaneously predicted and optimised using genetic algorithm optimisation. It was further proven that the Langmuir–Hinshelwood model can well predict propane dehydrogenation kinetics through lumping together all the possible dehydrogenation steps and also by assuming the surface reaction as the rate-determining step. A coke formation kinetic model has also shown appropriate results, confirming the experimental data by equal consideration of both monolayer and multilayer coke deposition kinetic orders and an exponential deactivation model.



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