A general model for moving-bed reactors with multiple chemical reactions, Part II: Effect of kinetic model

2013 ◽  
Vol 124 ◽  
pp. 67-74 ◽  
Author(s):  
Amir Rahimi ◽  
Arezou Niksiar
1973 ◽  
Vol 10 (3) ◽  
pp. 425-431
Author(s):  
Ta-Ming Fang

A previously developed set of kinetic model equations for a chemically-reacting gas is modified. By examining closely the H theorem, a new set of constraints is obtained. These conditions are then used to determine the inelastic collision parameters proposed in the model. The kinetic equations so obtained are able to produce exactly the same rate equations as prescribed by the actual chemical reactions.


Author(s):  
Dong Fu ◽  
Yan Chen ◽  
Chenn Q. Zhou

The blast furnace process is a counter-current moving bed chemical reactor to reduce iron oxides to iron, which involves complex transport phenomena and chemical reactions. The iron ore and coke are alternatively charged into the blast furnace, forming a layer by layer structural burden which is slowly descending in the counter-current direction of the ascending gas flow. A new methodology was proposed to efficiently simulate the gas and solid burden flow in the counter current moving bed in blast furnace shaft. The gas dynamics, burden movement, chemical reactions, heat and mass transfer between the gas phase and solid phase are included. The new methodology has been developed to explicitly consider the effects of the layer thickness thermally and chemically in the CFD model.


2011 ◽  
Vol 2011 (03) ◽  
pp. P03014 ◽  
Author(s):  
Giselle M Alves ◽  
Gilberto M Kremer ◽  
Wilson Marques Jr ◽  
Ana Jacinta Soares

PAMM ◽  
2005 ◽  
Vol 5 (1) ◽  
pp. 533-534 ◽  
Author(s):  
Florian Zus ◽  
Herbert Olivier

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