“…Assuming thermal equilibrium between fluid and particles, the energy balance for gas and solid phases is given by where K , is the effective axial thermal conductivity (Suzuki, 1990;Malek and Farooq, 1997).…”
The adsorption dynamics of a layered bed packed with activated carbon and zeolite 5A were studied experimentally and theoretically through breakthrough experiments and two-bed pressure swing adsorption (PSA) processes by using coke oven gas (56.4 vol. % H,; 26.6 vol. % CH,; 8.4 vol. % CO; 5.5 vol
“…Assuming thermal equilibrium between fluid and particles, the energy balance for gas and solid phases is given by where K , is the effective axial thermal conductivity (Suzuki, 1990;Malek and Farooq, 1997).…”
The adsorption dynamics of a layered bed packed with activated carbon and zeolite 5A were studied experimentally and theoretically through breakthrough experiments and two-bed pressure swing adsorption (PSA) processes by using coke oven gas (56.4 vol. % H,; 26.6 vol. % CH,; 8.4 vol. % CO; 5.5 vol
“…This choice was also found to provide a suitable compromise between minimizing the mag- 'Malek (1996). 'Malek and Farooq (1997a).…”
Section: Simulation Of Dual-sorbent Psa Processmentioning
confidence: 97%
“…As shown in Malek and Farooq (1997a) and Malek (1996), for the adsorption of C,-C, in activated carbon adsorbent, D,,,, = 0.0085 cm2/s, while for the same in silica gel adsorbent, D,,,,, = 0.0018 cm2/s.…”
Section: Simulation Of Dual-sorbent Psa Processmentioning
“…Several complex theoretical models have been proposed in the literature (Tien 1994;Brosillon et al 2001;Malek and Farooq 1997;Delage et al 2000;Pre et al 2002;Sircar and Hufton 2000) for simulating breakthrough curves. In this paper, the LDF model [equation (3)] linked to the mass balance in a portion of the bed [equation (2)] and the Langmuir model [equation (9)] have been applied for describing the equilibrium experimental data.…”
Section: Modelling Of Breakthrough Curvesmentioning
confidence: 99%
“…Thus, Brosillon et al (2001) investigated the kinetic performance of zeolites for VOC (n-heptane, n-octane, acetone and methyl ethyl ketone) abatement and observed that the effective diffusivity was constant regardless of the nature and amount of VOC adsorbed. Similarly, Malek and Farooq (1997) studied the kinetic behaviour of small VOC molecules (methane, ethane and propane) in their adsorption onto activated carbon and silica gel, and found that adsorbate transport inside the adsorbent occurred essentially by Knudsen and surface flow. However, none of these authors focused on modelling the adsorption of HCs onto zeolites and the relationship between the kinetic and equilibrium parameters and the structural characteristics of the adsorbent.…”
ABSTRACT:The modelling of breakthrough curves obtained in the adsorption of propene as a model compound onto different inorganic solids is described. All the runs were performed in a fixed bed at atmospheric pressure, employing a process temperature of 30 ºC and propene concentrations in the range 0.0022-0.0222 mol/Nm 3 . The experimental conditions were therefore similar to those observed in the initial flue gases of cold start engines. The work described was mainly focused on the study of the influence of the adsorbent characteristics (composition, porous structure and surface area) on the kinetics of the adsorption process. The equilibrium adsorption values were initially determined from the breakthrough curves and satisfactorily fitted by the Langmuir isotherm model. These values were then used together with experimental breakthrough curves to analyse the kinetic expressions obtained applying the Linear Driving Force (LDF) model to the dynamic adsorption process. Values of the masstransfer coefficient, surface and effective diffusion coefficients of propene have been calculated and are reported.
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