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| Parameter | Description | Units |
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| a | Specific particle surface | m2m-3 |
| aHi | Specific heat exchanger surface | m2m-3 |
| ap | Specific particle surface per unit volume bed | m2m-3 |
| A | Area | |
| AA | Placeholder variable used for Dubinin-Astakhov isotherm evaluation | |
| b | Kinetic Langmuir factor | bar-1 |
| cbi | Bulk gas phase concentration | kmolm-3 |
| ci | Molar concentration of component i | kmolm-3 |
| cmsi | Macropore gas phase concentration | kmolm-3 |
| csol | Concentration of solid phase reactant | kmolkg-1 |
| cpai | Specific heat capacity of adsorbed phase | MJkmol-1K-1 |
| cpcat | Specific heat capacity of catalyst | MJkg-1K-1 |
| cpg | Specific gas phase heat capacity at constant pressure | MJkmol-1K-1 |
| cps | Specific heat capacity of adsorbent | MJkg-1K-1 |
| cpW | Specific heat capacity of column wall | MJkg-1K-1 |
| cvg | Specific gas phase heat capacity at constant volume | MJkmol-1K-1 |
| DB | Bed diameter | m |
| Defc | Effective micropore diffusion coefficient | m2s-1 |
| Defp | Effective macropore diffusion coefficient | m2s-1 |
| Dek | Effective adsorbed phase diffusivity of component | m2s-1 |
| Dki | Knudsen diffusion coefficient of component | m2s-1 |
| Dmi | Mean molecular diffusion coefficient of component | MJkmol-1 |
| Eact | Activation energy for Arrhenius relationship | MJkmol-1 |
| Eii | Radial dispersion coefficient of component | m2s-1 |
| Ezi | Axial dispersion coefficient of component | m2s-1 |
| Hamb | Wall-ambient heat transfer coefficient | MWm2K-1 |
| HB | Height of adsorbent layer | m |
| Hi | Rate of change of heat of adsorbed phase | MJm-3s-1 |
| HR | Combined heats of homogenous and heterogeneous reactions | MJm-3s-1 |
| HRcat | Heat of catalytic reaction | MJkmol-1 |
| HRgas | Gas phase heat of reaction | MJkmol-1 |
| HTi | Heat of adsorption contribution to solid phase energy balance | MJm-3s-1 |
| HW | Gas-wall heat transfer coefficient | MJm-3s-1 |
| ΔHi | Heat of adsorption of component | MJkmol-1 |
| HTC | Gas-solid heat transfer coefficient | MJm-3s-1 |
| IP | Isotherm parameter, units depend on isotherm | |
| j | Colburn j-factor for heat or mass transfer | |
| Jads,i | Mass transfer rate of component owing to adsorption | kmolm-3s-1 |
| Jcat,reac,i | Mass transfer rate of component owing to heterogeneous catalytic reactions | kmolm-3s-1 |
| Jgas, reac ,i | Mass transfer rate of component owing to homogenous, gas phase reactions | kmolm-3s-1 |
| Ji | Mass transfer rate of component to/from adsorbent | kmolm-3s-1 |
| k0,i | Pre-exponential factor for Arrhenius relationship | ms-1 |
| k0P,i | Pre-exponential factor for pressure dependent Arrhenius relationship | ms-1 |
| kfi | Film mass transfer coefficient of component | ms-1 |
| kfi | Gas phase thermal conductivity | MWm-1K-1 |
| kgr | Effective radial gas phase thermal conductivity | MWm-1K-1 |
| ki | Effective, lumped mass transfer coefficient of component | s-1 |
| ks | Solid thermal conductivity | MWm-1K-1 |
| kgs | Effective axial gas phase thermal conductivity | MWm-1K-1 |
| ksr | Effective radial solid phase thermal conductivity | MWm-1K-1 |
| ksg | Effective axial solid phase thermal conductivity | MWm-1K-1 |
| kW | Thermal conductivity of column wall | MWm-1K-1 |
| Kmac | Macropore mass transfer coefficient | s-1 |
| Kmic | Micropore mass transfer coefficient | s-1 |
| Kp | Darcy’s constant | barsm-2 |
| Kpi | Macropore diffusion coefficient | m2s-1 |
| L | Length of horizontal bed | m |
| M | Molecular weight | kgkmol-1 |
| MTCg | Gas film mass transfer coefficient | s-1 |
| MTCs | Solid film mass transfer coefficient | s-1 |
| P | Pressure | bar |
| Psat | Saturation pressure | bar |
| QHi | Heat transfer rate to internal heat exchanger | MJm-2s-1 |
| r | Radial coordinate (in packed bed or particle) | m |
| rc | Microparticle (crystal) radius | m |
| rp | Particle radius | m |
| R | Universal gas constant | barm-3kmol-1K-1 |
| Rcat | Catalytic reaction rate | kmolkg-1s-1 |
| Rgas | Gas phase reaction rate | kmolm-3s-1 |
| Rsol | Solid phase reaction rate | kmolkg-1s-1 |
| t | Time | s |
| tcycle | Adsorption cycle time | s |
| T | Temperature | K |
| T0 | Initial temperature | K |
| Tamb | Ambient temperature | K |
| Tc | Critical temperature | K |
| Ts | Solid phase temperature | K |
| Tg | Gas phase temperature | K |
| THi | Heat exchange medium temperature | K |
| TW | Wall temperature | K |
| Tort | Adsorbent tortuosity | |
| vg | Gas phase superficial velocity | ms-1 |
| Wi | Loading | kmolkg-1 |
| Wi0 | Pure component loading of component | kmolkg-1 |
| yi | Mole fraction of component in the gas phase | kmolkg-1 |
| z | Axial coordinate | m |
| Greek symbols | | |
| ϵi | Bed (interparticle) voidage | m3 m-3 |
| ϵp | Intraparticle voidage | m3 m-3 |
| μ | Dynamic viscosity | N s m-2 |
| Ω | Parameter in Glueckauf expression | |
| ψ | Particle shape factor | |
| ρb | Bed packing density | kg m-3 |
| ρg | Gas phase molar density | kmol km-3 |
| ρp | Particle density | kmol km-3 |
| ρs | Adsorbent bulk density | kg m-3 |
| Subscripts | | |
| b | Bulk or packed bed | |
| F | Feed stream | |
| g, s | Gas and solid phase | |
| i | Component water () or ethanol () | |
| p | Particle | |
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