Generic placeholder image

Recent Innovations in Chemical Engineering

Editor-in-Chief

ISSN (Print): 2405-5204
ISSN (Online): 2405-5212

Research Article

Diffusion and Surface Reaction in Porous Cubical Catalyst: A Mathematical Approach

Author(s): Sourav Ghosh and Dipankar Pal*

Volume 15, Issue 1, 2022

Published on: 21 January, 2022

Page: [60 - 69] Pages: 10

DOI: 10.2174/2405520415666211229122346

Price: $65

conference banner
Abstract

Background: Catalysts are the most vital part of any chemical industry. Catalyst is a substance that affects the rate of reaction, but the catalyst itself does not take part in the reaction. Catalysts offer different pathways of reaction by diffusing the reactant inside it to provide a large surface area within a small volume, thus, lowering the activation energy of molecules for reaction. Most of the catalytic reactions take place in a liquid- solid or gas-solid interface where catalysts are mostly porous in nature. Spherical and cubic-shaped catalyst particles are commonly used in different industries.

Methods: In the first phase of the present study, the physics behind the diffusion inside the catalyst pellet has been discussed. In the second part, governing differential equations have been established at a steady-state condition. For solving the differential equation, the equation is made dimensionless. Physical boundary conditions were used to solve the diffusion equation. The assumption of writing the differential equation of the reaction is elementary. Then, the Thiele modulus is derived in terms of the reaction and geometrical parameter (Length).

Results and Conclusion: In the third part, the differential equation is solved for firstorder reaction with some constant values of the Thiele modulus, and three-dimensional plots are obtained using numerical analysis. After that, the obtained Thiele modulus and effectiveness factor plot are compared to draw the conclusion of rate limiting reaction and internal diffusion.

Keywords: Catalyst, diffusion, thiele modulus, effectiveness factor, activation energy, surface area, geometrical parameter, numerical analysis, reaction rate.

« Previous
Graphical Abstract

[1]
Aris R. The mathematical theory of diffusion and reaction in permeable catalysts. The theory of Steady StateClarendon, Oxford. 1975.
[2]
Thiele EW. Relation between catalytic activity and size of particle. Ind Eng Chem 1939; 31: 916-20.
[http://dx.doi.org/10.1021/ie50355a027]
[3]
Magyari E. Exact analytical solution of a nonlinear reaction-diffusion model in porous catalysts. Chem Eng J 2008; 143: 167-71.
[http://dx.doi.org/10.1016/j.cej.2008.03.018]
[4]
Wakao N, Smith JM. Diffusion and reaction in porous catalysts. Ind Eng Chem Fundam 1964; 3(2): 123-7.
[http://dx.doi.org/10.1021/i160010a007]
[5]
Abbasbandy S. Approximate solution for the nonlinear model of diffusion and reaction in porous catalysts by means of the homotopy analysis method. Chem Eng J 2008; 136(2-3): 144-50.
[http://dx.doi.org/10.1016/j.cej.2007.03.022]
[6]
Hoogschagen J. Diffusion in porous catalysts and adsorbents. Ind Eng Chem 1955; 47(5): 906-12.
[http://dx.doi.org/10.1021/ie50545a016]
[7]
Roberts GW, Satterfield CN. Effectiveness factor for porous catalysts. Langmuir-hinshelwood kinetic expressions. Ind Eng Chem Fundam 1965; 4(3): 288-93.
[http://dx.doi.org/10.1021/i160015a009]
[8]
Robinson DM, Go YB, Greenblatt M, Dismukes GC. Water oxidation by λ-MnO2: catalysis by the cubical Mn4O4 sub-cluster obtained by delithiation of spinel LiMn2O4. J Am Chem Soc 2010; 132(33): 11467-9.
[http://dx.doi.org/10.1021/ja1055615] [PMID: 20672802]
[9]
Silva HA, Aguiar LG. Mathematical modeling of heterogeneous catalysis involving polymer-supported catalysts. Kinet Catal 2017; 58: 211-7.
[http://dx.doi.org/10.1134/S0023158417020112]
[10]
Szukiewicz MK. Study of reaction–diffusion problem: modeling, exact analytical solution, and experimental verifica-tion. SN Appl Sci 2020; 2: 1253.
[http://dx.doi.org/10.1007/s42452-020-3045-0]
[11]
Cao S, Tao FF, Tang Y, Li Y, Yu J. Size- and shape-dependent catalytic performances of oxidation and reduction reac-tions on nanocatalysts. Chem Soc Rev 2016; 45(17): 4747-65.
[http://dx.doi.org/10.1039/C6CS00094K] [PMID: 27276189]
[12]
Yan F, Li C, Liang X, Guo S, Yang F, Li C. Baeyer-villiger reaction in different catalysis. Recent Pat Chem Eng 2013; 6(1): 43-56.
[http://dx.doi.org/10.2174/2211334711306010004]
[13]
Al Dwairi Reyad A, Al-Rawajfeh Aiman E. Recent patents of natural zeolites applications in environment, agriculture and pharmaceutical industry. Recent Pat Chem Eng 2012; 5(1): 20-7.
[http://dx.doi.org/10.2174/2211334711205010020]
[14]
Vanesa C-C, Rosa MM-A. Advances in metal-organic frameworks for heterogeneous catalysis. Recent Pat Chem Eng 2011; 4(1): 1-16.
[http://dx.doi.org/10.2174/2211334711104010001]
[15]
Son WJ, Kim J, Kim J, Ahn WS. Sonochemical synthesis of MOF-5. Chem Commun (Camb) 2008; (47): 6336-8.
[http://dx.doi.org/10.1039/b814740j] [PMID: 19048147]
[16]
Scott Fogler H. Elements of chemical reaction engineering Prentice Hall. USA: University of Michigan 2020.

Rights & Permissions Print Cite
© 2024 Bentham Science Publishers | Privacy Policy