CFD Simulation of Hydrodynamics and Methanation Reactions in a Fluidized-Bed Reactor for the Production of Synthetic Natural Gas

2014 ◽  
Vol 53 (22) ◽  
pp. 9348-9356 ◽  
Author(s):  
Yefei Liu ◽  
Olaf Hinrichsen
2012 ◽  
Vol 26 (4) ◽  
pp. 2058-2067 ◽  
Author(s):  
Abolhasan Hashemi Sohi ◽  
Ali Eslami ◽  
Amir Sheikhi ◽  
Rahmat Sotudeh-Gharebagh

2012 ◽  
Vol 586 ◽  
pp. 274-281
Author(s):  
Mohammad Kazemeini ◽  
Reza Maleki ◽  
Moslem Fattahi

The FT reaction involves the conversion of syngas which is derived from natural gas or coal to different kinds of products according to the operating conditions and the type of the catalyst. In other words, it is a practical way to convert solid fuel (coal) and natural gas to various hydrocarbons (C1-C60) and oxygenates such as alkanes, alkenes etc. The main products of the reaction are naphtha and gasoline. This paper deals with developing a proper product distribution model for FT process using the appropriate kinetic model, optimizing the respective rate constants while applying them in product distribution equations. The results revealed only 8.09% deviations from the olefin experimental data and 10.27% deviations from the paraffin experimental data being acceptable when compared with previous open literature data.


2019 ◽  
Vol 201 ◽  
pp. 112143 ◽  
Author(s):  
Zhenwei Li ◽  
Hongpeng Xu ◽  
Wenming Yang ◽  
Anqi Zhou ◽  
Mingchen Xu

Author(s):  
Vitor Alberto Lemes Monteiro ◽  
Maurício Guilherme Alves dos Reis ◽  
Luciano Infiesta ◽  
Solidônio Carvalho

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