2004
DOI: 10.1016/j.ces.2003.08.025
|View full text |Cite
|
Sign up to set email alerts
|

Approximate model for diffusion and reaction in a porous pellet and an effectiveness factor

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
5

Citation Types

2
27
0

Year Published

2008
2008
2023
2023

Publication Types

Select...
7
1

Relationship

0
8

Authors

Journals

citations
Cited by 17 publications
(29 citation statements)
references
References 8 publications
2
27
0
Order By: Relevance
“…CO þ H 2 O4CO 2 þ H 2 ð À DH 298 ¼ 41:2 kJ=molÞ (3) CH 4 þ 2H 2 O4CO 2 þ 4H 2 ; ð À DH 298 ¼ À165 kJ=molÞ (4) For reactions (2)e(4) a LangmuireHinshelwood mechanism can be established using NiMgAl 2 O 4 as a catalyst [2], which was used in the current work. Following Hill's method [3] it can be proven that only 2 reactions are independent, so that only two fractional conversions can be used, namely that of CO 2 and CH 4 :…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…CO þ H 2 O4CO 2 þ H 2 ð À DH 298 ¼ 41:2 kJ=molÞ (3) CH 4 þ 2H 2 O4CO 2 þ 4H 2 ; ð À DH 298 ¼ À165 kJ=molÞ (4) For reactions (2)e(4) a LangmuireHinshelwood mechanism can be established using NiMgAl 2 O 4 as a catalyst [2], which was used in the current work. Following Hill's method [3] it can be proven that only 2 reactions are independent, so that only two fractional conversions can be used, namely that of CO 2 and CH 4 :…”
Section: Introductionmentioning
confidence: 99%
“…Usually the particles are large so that the pressure drop is small, which leads to high mass transfer resistances in the particles [4]. For reactions (2)e(4) in industrial practice the effectiveness factors are very low (<0.03) due to high diffusional limitations in the solid porous network [5,6].…”
Section: Introductionmentioning
confidence: 99%
“…Moreover, the need of solving the partial differential equations (PDEs) of the mass balances in the particle, which are coupled to the corresponding mass balances in the fluid phase, can be avoided since pseudo homogeneous systems outcomes. An important number of works exists where the effectiveness factor is studied and approximate expressions are developed to obtain fast estimations, or to extend the approach to different particle geometries or chemical reaction kinetics (Bischoff, 1965;Gonzo et al, 1988;Gottifredi et al, 1981;Gottifredi and Gonzo, 2005;Haynes, 1986;Lee and Kim, 2006;Szukiewicz and Petrus, 2004).…”
Section: Introductionmentioning
confidence: 99%
“…Due to substantial inaccuracies with this equation, a number of other approximate kinetic equations were proposed. They referred both to the process of diffusion with adsorption [2][3][4][5] and diffusion with chemical reaction [6][7][8][9][10][11][12][13][14][15][16].…”
Section: Introductionmentioning
confidence: 99%