Adiabatic adsorption

Equilibrium vapor pressure of bulk liquid Relative pressure, p/p 0 Statistical mechanical partition function Density in molecules/cubic centimeter Gas constant per mole Number of moles of adsorbed gas Number of moles of adsorbent Isosteric heat of adsorption Differential heat of adsorption Isothermal heat of adsorption Adiabatic heat of adsorption... 

FIG. 16-22 Transition paths in Cj, T plane for adiabatic adsorption and thermal regeneration. 

Because of this heat generation, when adsorption takes place in a fixed bed with a gas phase flowing through the bed, the adsorption becomes a non-isothermal, non-adiabatic, non-equilibrium time and position dependent process. The following set of equations defines the mass and energy balances for this dynamic adsorption system [30,31] ... 

To determine correlation between (t) and nd, therefore, to find out the type of dependence f let us consider the occupation kinetics for ASS levels by free charge carriers. The capturing of charge carriers occurring during transition of adsorption particles into the charged form will be considered, as usual, in adiabatic approximation, i.e. assuming that at any moment of time there is a quasi-equilibrium and the system of crystallites is characterized by immediate equilibrium values and L inside the conduction (valence) band. 

The application of open sorption systems can provide dehumidification by the adsorption of water vapor and sensible cooling by adiabatic humidification (after a cold recovery for the dried air) at temperatures between 16 °C and 18 °C. Conventional systems have to reach temperature as low as 6 °C or lower in order to start dehumidification by condensation. For comfort reasons this cold air has to be heated up to about 18 °C before released into the building. This shows that open sorption systems can provide in general an energetically preferable solution. 

A survey of the literature shows that although very different calorimeters or microcalorimeters have been used for measuring heats of adsorption, most of them were of the adiabatic type, only a few were isothermal, and until recently (14, 15), none were typical heat-flow calorimeters. This results probably from the fact that heat-flow calorimetry was developed more recently than isothermal or adiabatic calorimetry (16, 17). We believe, however, from our experience, that heat-flow calorimeters present, for the measurement of heats of adsorption, qualities and advantages which are not met by other calorimeters. Without entering, at this point, upon a discussion of the respective merits of different adsorption calorimeters, let us indicate briefly that heat-flow calorimeters are particularly adapted to the investigation (1) of slow adsorption or reaction processes, (2) at moderate or high temperatures, and (3) on solids which present a poor thermal diffusivity. Heat-flow calorimetry appears thus to allow the study of adsorption or reaction processes which cannot be studied conveniently with the usual adiabatic or pseudoadiabatic, adsorption calorimeters. In this respect, heat-flow calorimetry should be considered, actually, as a new tool in adsorption and heterogeneous catalysis research. 

Figure 9.7 Adiabatic potential-energy surface for the adsorption of an iodide ion on Pt(100) at the pzc the original figure from [7] has been changed slightly for greater clarity. Contour lines are drawn for energies from -0.8 eV to 0 eV in steps of 0.1 eV. The white dashed line shows a possible reaction path.

Figure 17.23. Idealised distributions of temperature and concentrations during adiabatic adsorption...

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