1991
DOI: 10.1002/aic.690371015
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Concentration dependence of surface diffusion and zeolitic diffusion

Abstract: Surface diffusion, that is, diffusion of adsorbed molecules or atoms on surfaces, has long been investigated (Kapoor et al., 1989). Diffusion of sorbate in zeolite, called zeolitic diffusion, has attracted a special interest recently because of the increasing importance of zeolite in separation and catalysis. One of the most intriguing aspects of both surface diffusion and zeolitic diffusion is the strong dependence of diffusivity (Fickian diffusivity) on sorbate concentration. However, seemingly different con… Show more

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Cited by 201 publications
(113 citation statements)
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“…In this work, with the effective diffusion coefficient ( ) determined from the homogeneous particle diffusion model and pore diffusion coefficient reported by Ocampo-Perez et al [9], and show the same order of magnitude of effective diffusion coefficients (in Table 2) but much lower than the according pore diffusion coefficients (in Table 3), which indicates a significant effect of surface diffusion on the micropore adsorption kinetics. A trend shows the surface diffusion coefficient increases with temperature from 25 to 55 0 C and this is more prominent for MN 500, supporting the hypothesis that surface diffusion is an activated mass transfer process, where the increase of temperature facilitates molecular hopping between distinct, energetically favourable adsorption sites on the surface [47,75,76]. The surface diffusion coefficient was reported to increase with adsorbent loading, hence is expected to increase with initial adsorbent concentration according to Darken theory [77], although this trend is not well defined in our case, possibly due to the small concentration differences (100 to 200 mg/L).…”
Section: Substituting Equations 14 and 15 Into Equation 13supporting
confidence: 53%
“…In this work, with the effective diffusion coefficient ( ) determined from the homogeneous particle diffusion model and pore diffusion coefficient reported by Ocampo-Perez et al [9], and show the same order of magnitude of effective diffusion coefficients (in Table 2) but much lower than the according pore diffusion coefficients (in Table 3), which indicates a significant effect of surface diffusion on the micropore adsorption kinetics. A trend shows the surface diffusion coefficient increases with temperature from 25 to 55 0 C and this is more prominent for MN 500, supporting the hypothesis that surface diffusion is an activated mass transfer process, where the increase of temperature facilitates molecular hopping between distinct, energetically favourable adsorption sites on the surface [47,75,76]. The surface diffusion coefficient was reported to increase with adsorbent loading, hence is expected to increase with initial adsorbent concentration according to Darken theory [77], although this trend is not well defined in our case, possibly due to the small concentration differences (100 to 200 mg/L).…”
Section: Substituting Equations 14 and 15 Into Equation 13supporting
confidence: 53%
“…Apparently, the stretched exponential approximation predicted by Kinetic Monte Carlo simulations [12] seems to be a slightly better fit for the experimental data: first-order decay with the fitted coefficient b ¼ 1=3:239. Even though expression 17 failed to describe the data for 3-methylpentane in silicalite, the fitted value of ¼ 10:02 is in line with the values found by Chen and Yang [18] for the diffusion of thriethylamine in 13X zeolite and for benzene in ZSM-5, that are equal to 10.2 and 2.11 respectively.…”
Section: Concentration Dependence Of the Diffusivitysupporting
confidence: 82%
“…The self-diffusivity at zero coverage depends on the dimension of the lattice only, because there are no interactions between the molecules. (3) From calculations based on transition state theory, a general formula was derived to describe the concentration dependence of surface and zeolitic diffusions [18]:…”
Section: Concentration Dependence Of the Diffusivitymentioning
confidence: 99%
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“…This observation is consistent with the reports by Pillalamarry et al [28], while in opposition with the results mentioned above. Based on this, the reduction in methane diffusivity with pressure may be attributed to two reasons: (1) the degree of pore blockage by methane molecule increase with increasing surface coverage (adsorbed volume), making methane molecules difficult to diffuse into adsorption sites through pathways [59]; and (2) as methane diffuses into adsorption sites, the concentration gradient between bulk particles and their surfaces decrease with increasing pressures and adsorbed volume, slowing methane diffusion. It is apparent that there is an evident negative correlation between macropore diffusivity and pressure lower than 3-4 MPa (Figure 9a), while the micropore diffusivity only showed a gentle decreasing trend with pressure (Figure 9b), with the exception of sample YY2-2 and CY1-1.…”
Section: Effect Of Pressure and Surface Coverage On Methane Diffusivimentioning
confidence: 99%