Non-isothermal adsorption in a bidisperse adsorbent pellet
β Scribed by L.M. Sun; F. Meunier
- Publisher
- Elsevier Science
- Year
- 1987
- Tongue
- English
- Weight
- 875 KB
- Volume
- 42
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
The kinetics of adsorption in bidisperse pellets has been largely studied under isothermal condition. But due to large heat of adsorption, the isothermal models may lead to erroneous results. The present paper proposes a non-isothermal bidisperse model, taking into account two scale mass diffusion (macro-micropore diffusion) and one scale heat diffusion (the temperature within the microparticles is assumed uniform). This model is solved numerically, yielding the sorption uptake and temperature evolution. It turns out that considering the simultaneous macro-micropore diflusion is only necessary for 10m6 < a < lo-' (01 is the ratio of macropore and micropore diffusional resistances). The macropore diffusion should he rate limiting if the parameter a > lo-' and the micropore diffusion become rate limiting if 01 < 10e6. On the other hand, heat effect may make the isothermal assumption quite erroneous when the diffusion in the macropores and micropores is rapid and the heat transfer between the adsorbent and the ambient sorbate is small.
π SIMILAR VOLUMES
To be realistic, diffusion in bidisperse porous structures is often considered in terms of macropore diffusion and micropore diffusion. In this approach the diffusivity and the mass balance are defined separately for each pore system. Ruckenstein et al. (1971) and many investigators (Haynes and Sarm
## Abshct -A theoretical analysis of an adiabatic non-isothermal single-pellet diffusion reactor shows that nonisothermal effects can alter the value of the centerplane concentration. Deviation from isothermal behavior is significant under exothermic conditions where multiplicity of solutions can
In this study, a geometrical model is combined with the network of pores analogue to yield a structural-phenomenological description for diffusion and adsorption in pellets compacted from bidisperse and non-porous grains. Simulation results from both steady-state (single-pellet) and transient (chrom
FIG. 1. Photograph of a random sample of CC14 drops ~ukqJaulaL\*u WLLII a l.
Multicomponent adsorption in a bidisperse pellet has been studied. The interferemx between components is included both through the adsorption equilibrium and through ditTusion in both macropores and micropores. By the application of moment analysis and matrix operations, the moment solution of the s