scholarly journals Novel Membrane Reactor with Filamentous Catalytic Bed for Propane Dehydrogenation

2001 ◽  
Vol 40 (23) ◽  
pp. 5234-5239 ◽  
Author(s):  
O. Wolfrath ◽  
L. Kiwi-Minsker ◽  
A. Renken
2017 ◽  
Vol 17 (1) ◽  
pp. 113 ◽  
Author(s):  
Kamran Ghasemzadeh ◽  
Milad Mohammad Alinejad ◽  
Milad Ghahremani ◽  
Rahman Zeynali ◽  
Amin Pourgholi

This study presents a 2D-axisymmetric computational fluid dynamic (CFD) model to investigate the performance Pd membrane reactor (MR) during propane dehydrogenation process for hydrogen production. The proposed CFD model provided the local information of temperature and component concentration for the driving force analysis. After investigation of mesh independency of CFD model, the validation of CFD model results was carried out by other modeling data and a good agreement between CFD model results and theoretical data was achieved. Indeed, in the present model, a tubular reactor with length of 150 mm was considered, in which the Pt-Sn-K/Al2O3 as catalyst were filled in reaction zone. Hence, the effects of the important operating parameter (reaction temperature) on the performances of membrane reactor (MR) were studied in terms of propane conversion and hydrogen yield. The CFD results showed that the suggested MR system during propane dehydrogenation reaction presents higher performance with respect to once obtained in the conventional reactor (CR). In particular, by applying Pd membrane, was found that propane conversion can be increased from 41% to 49%. Moreover, the highest value of propane conversion (X = 91%) was reached in case of Pd-Ag MR. It was also established that the feed flow rate of the MR is to be the one of the most important factors defining efficiency of the propane dehydrogenation process.


AIChE Journal ◽  
1993 ◽  
Vol 39 (3) ◽  
pp. 526-529 ◽  
Author(s):  
Z. D. Ziaka ◽  
R. G. Minet ◽  
T. T. Tsotsis

AIChE Journal ◽  
2017 ◽  
Vol 63 (10) ◽  
pp. 4519-4531 ◽  
Author(s):  
Seung-Won Choi ◽  
David S. Sholl ◽  
Sankar Nair ◽  
Jason S. Moore ◽  
Yujun Liu ◽  
...  

Author(s):  
Shailesh Dangwal ◽  
Anil Ronte ◽  
Ghader Mahmodi ◽  
Payam Zarrintaj ◽  
Jong Suk Lee ◽  
...  

2005 ◽  
Vol 5 (2) ◽  
pp. 176
Author(s):  
Azis Trianto ◽  
Yazid Bindar ◽  
Noezran Noezran

Propane dehydrogenation is a promising route for producing propylene to replace traditional cracking methods. A membrane reactor offers a possibility to produce not only chemical grade but also polymer grade of propylene. The purpose of the present study is to evaluate the performance of a Modified Porous Membrane Reactor (MPMR) in producing these two propylene grades simultaneously. The study involves evaluations based on thermodynamics and process flow sheeting. The performance of this reactor is compared to that of conventional reactor. At first, the thermodynamics is conducted using minimum Gibb's Energy approach. Then the process flow sheeting evaluation is built using the HYSYS simulator. The effect of inert gas (steam) concentration in both sweep and feed sides is investigated. The thermodynamics study results optimum temperature and inert gas concentration to obtain these two grades of propylene simultaneously. The propylene with polymer grade above 99% is produced from the sweep side outlet. The propylene with chemical grade is produced from the feed side outlet. The simultaneous production of these two grades of propylene has benefit in vanishing propane-propylene splitter. Keywords: Membrane reactor, porous membrane, propane dehydrogenation, propylene production, and process simulation.


Sign in / Sign up

Export Citation Format

Share Document