1968
DOI: 10.1016/0009-2509(68)87056-3
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Gas dispersion in packed beds

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Cited by 405 publications
(141 citation statements)
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“…The axial dispersion coefficient is at most proportional to the interstitial gas velocity (Edwards and Richardson, 1968;Suzuki and Smith, 1972), so at high values of U,, the axial dispersion term is negligible. Thus, the micropore diffusion coefficient can be obtained from the intercept of plots of dU0/2L vs. l/U: (referred to as variance plots).…”
Section: )mentioning
confidence: 97%
“…The axial dispersion coefficient is at most proportional to the interstitial gas velocity (Edwards and Richardson, 1968;Suzuki and Smith, 1972), so at high values of U,, the axial dispersion term is negligible. Thus, the micropore diffusion coefficient can be obtained from the intercept of plots of dU0/2L vs. l/U: (referred to as variance plots).…”
Section: )mentioning
confidence: 97%
“…the semi-empirical correlation proposed by Edwards and Richardson (1968) was used to estimate the axial dispersion coe$cient D X . The catalyst e!ectiveness factor, G , was set as unity for the crushed catalyst used in this work; see Section 4 for details.…”
Section: Governing Equationsmentioning
confidence: 99%
“…[17][18][19][20][21] Many other fluid flow and mass transfer research also involve the determination of concentration distribution. Use of conductivity probes is one of the techniques, which has been used by few researchers.…”
Section: Concentration Experimentsmentioning
confidence: 99%