Last edited by Dulkis
Wednesday, July 15, 2020 | History

2 edition of Analysis and measurement of diffusion in porous catalysts. found in the catalog.

Analysis and measurement of diffusion in porous catalysts.

Homoud Abdullah Al-Roobah

Analysis and measurement of diffusion in porous catalysts.

by Homoud Abdullah Al-Roobah

  • 382 Want to read
  • 2 Currently reading

Published by University of Salford in Salford .
Written in English


Edition Notes

PhD thesis, Chemical Engineering.

SeriesD39629/82
ID Numbers
Open LibraryOL19686830M

An experimental method was developed to study the adsorption and diffusion of the reactant, and the product, reacting on porous catalysts by simultaneoTo study the effect of reaction on the. Diffusion of unrestricted liquids was analysed using the pulsed gradient stimulated echo (PGSTE) sequence. 35 To minimise the effects of background magnetic field gradients (so-called internal gradients 36) the diffusion of liquids confined to the porous catalysts was analysed using the alternating pulsed gradient stimulated echo (APGSTE.

In a variety of catalytic processes dealing with porous catalysts, bidisperse solids arc used. In such systems, it is important to know the adsorption rate together with the diffusion rate in the. Mathematical models of reaction and transport in porous catalyst on three different scales (nano, micro, and macro) are presented. Methodology is demonstrated on CO oxidation in porous Pt/γ-Al2O3.

  Measurement of the Effective Diffusivity in Porous Media by the Diffusion Cell Method. Catalysis Reviews , 38 (2), DOI: / S. Satoh, I. Matsuyama, K. Susa. Diffusion of gases in porous silica gel.   A cautionary note on the interpretation of the above described Koutechky–Levich analysis or of RRDE measurements is suggested here, as it was shown that the apparent number of electron transferred in the ORR deduced from RRDE measurements can depend on electrode thickness. 7, 43, 44 For example, Fe–N–C-based catalysts were shown to.


Share this book
You might also like
Modeling inventories over the business cycle

Modeling inventories over the business cycle

Marilyn Monroe.

Marilyn Monroe.

Health, shellfish

Health, shellfish

constitution of community in legal sites

constitution of community in legal sites

The science of non verbal communication

The science of non verbal communication

historical sketch of the Redwood library and athenaeum, in Newport, Rhode Island.

historical sketch of the Redwood library and athenaeum, in Newport, Rhode Island.

Handbook on the Education Department.

Handbook on the Education Department.

The decisive moment

The decisive moment

Luther F. Palmer.

Luther F. Palmer.

Quick ones

Quick ones

Defoe companion

Defoe companion

Induction and orientation of staff

Induction and orientation of staff

Booklet of sonnets

Booklet of sonnets

Modern Mongolian

Modern Mongolian

Analysis and measurement of diffusion in porous catalysts by Homoud Abdullah Al-Roobah Download PDF EPUB FB2

In the long-time region the large crystals become dominant and the slope of the response curve of model B becomes less than that of model A indicating a lar- (14) ger diffusional time constant. Measurement of diffusion in porous catalysts A w Cited by: 8.

Analysis of diffusion in macroporous media in terms of a porosity, a tortuosity and a constrictivity factor. International Journal of Heat and Mass Transfer17 (9), DOI: /(74) R.

Jackson. On the limit of bulk diffusion control and high permeability in porous catalyst Cited by: Diffusion and convection in porous catalysts.

New York, N.Y.: American Institute of Chemical Engineers, (OCoLC) Material Type: Conference publication: Document Type: Book: All Authors / Contributors: Ian A Webster; William C Strieder; John L Anderson; American Institute of Chemical Engineers.

Annual Meeting. A modified Wicke-Kallenbach diffusion cell has been employed to measure the effective diffusivities of gases present in steam reforming in porous catalyst pellets within the temperature range of – K and at pressures from 1 to 10 by:   A series of porous Al 2 O 3 pellet with different microstructures were prepared and characterized.

The effective diffusion coefficient of CO 2 was predicted using the random pore model. The effective diffusion coefficient of CO 2 was predicted by computer simulation.

Experimental and calculated values were in good : H. Yamada, T. Tagawa, S. Nagao, S. Kato. The rate of swimming is a function of the rate of diffusion into the tail. Therefore, consider only diffusion in the tail.

Mole Balance. Constitutive Equation and Rate Law. Boundary Conditions. at z = 0, C A = C A0. at z = L, dC A / dz = 0. Combine and Put the Equation in Dimensionless Form. When = 0, then = 1. When = 1, then. Jan P. Sørensen, Warren E. Stewart, Collocation analysis of multicomponent diffusion and reactions in porous catalysts, Chemical Engineering Science, /(82), 37, 7.

Analysis of the effect of internal diffusion is complicated by such factors as the shape of the particles, the distribution in size and shape of the pores, the total volume of the pores with respect to the particle volume (porosity, h), the depth to which the pores penetrate the particles (e.g., pellicular particles have only a thin layer of.

Reaction and Diffusion in a Porous Catalyst Pellet by Richard K. Herz Solid catalysts are often called "heterogeneous catalysts" meaning that they are in a different phase from fluid reactants and products.

The ease of separating solid catalysts from reactants and products gives them an and Ω from measurements of r A,obs.

surface of solids or porous particles, which are surrounded by gas or liquid • If the chemical reaction proceeds very fast, the overall rate may be controlled by the transport of reactand from the fluid to the external surface of the catalyst particle or by diffusion inside the pores of the catalyst particle.

Claudia M. Bidabehere, Ulises Sedran, Use of stirred batch reactors for the assessment of adsorption constants in porous solid catalysts with simultaneous diffusion and reaction. Theoretical analysis, Chemical Engineering Science, /, 61, 6, (), ().

Diffusion and flow rates through porous catalysts were measured under the conditions of finite pressure gradients for single‐ and two‐component systems.

For large pore (low density) alumina pellets the diffusion rate counter to the pressure gradient was severely depressed, while for small pore Vycor the pressure gradient had little effect. Klaus P. Möller, Cyril T. O'Connor, The measurement of diffusion in porous catalysts using a CSTR, Chemical Engineering Science, /(95), 51, 13, (), ().

Crossref Dong-Ik Song, The second vs. the third moment matching between diffusion models for dynamic adsorber, Korean Journal of Chemical Engineering, Atoms and molecules in all states of matter are subject to continuous irregular movement.

This process, referred to as diffusion, is among the most general and basic phenomena in nature and determines the performance of many technological processes. This book provides an introduction to the fascinating world of diffusion in microporous solids.

Jointly written by three well-known researchers in. The subject of reaction and diffusion in porous catalysts is now a well established branch of knowledge discussed in several books such as by Aris and Jackson.

Its practical importance has long been recognized since the pioneer work by Thiele. Abstract Accuracy in the effective diffusion coefficient of the gas diffusion layer (GDL)/microporous layer (MPL) is important to accurately predict the mass transport limitations for high current density operation of polymer electrolyte membrane (PEM) fuel cells.

All the previous studies regarding mass transport limitations were limited to pure GDLs, and experimental analysis of the impact of. Klaus P. Möller, Cyril T. O'Connor, The measurement of diffusion in porous catalysts using a CSTR, Chemical Engineering Science, /(95), 51, 13, (), ().

Crossref. Schematic of a porous catalyst C C AS 0 rR Typical concentration profiles within the catalyst dr dC Diffusive flux in the catalyst =−D eA D eA effective or intraparticle diffusion coefficient of species A in the catalyst.

= A medium property; not a unique species property. Abstract When heterogeneous chemical reactions take place in porous catalysts, mass transport can occur by bulk diffusion, Knudsen diffusion, and convective transport.

Previous studies of these. Abstract. In this chapter, the necessary parameters for both rotating disk electrode/rotating ring-disk electrode analysis in oxygen reduction reaction study, such as O 2 solubility, O 2 diffusion coefficient and the viscosity of the aqueous electrolyte solutions are discussed in depth in terms of their definitions, theoretical background, and experiment measurements.

TY - BOOK. T1 - Design of porous nanostructured solid catalysts. AU - Abildstrøm, Jacob Oskar. PY - Y1 - N2 - This thesis aims at developing and characterize novel porous nanostructered materials for heterogeneous catalysis.

The catalysts are prepared with the goals of increased activity and stability in mind. Diffusion and Reaction in Catalyst Pellets with Bidisperse Pore Size Distribution.

Industrial & Engineering Chemistry Research37 (6), DOI: /iet. Susan M. Richardson, Hiroshi Nagaishi, and, Murray R. Gray. Initial Coke Deposition on a NiMo/γ-Al2O3 Bitumen Hydroprocessing Catalyst.Analysis and measurement of diffusion in porous catalysts. Author: Al-Rqobah, A. ISNI: Awarding Body: University of Salford Current Institution: University of Salford Date of Award: Availability of Full Text: Access from EThOS.