No abstract

The adsorption equilibrium and regeneration efficiency of n-hexane, methyl ethyl ketone (MEK), and toluene under supercritical CO2 on an activated carbon fiber were experimentally determined. When the densities of the supercritical fluids were fixed at 0.32, 0.45, and 0.62 g/cm3, the Langmuir model agreed with the experimental isotherms at the temperatures 308, 318, and 328 K. As the concentration of adsorptive in supercritical CO2 was kept constant, the crossover of the equilibrium loading at different temperatures was observed at relatively high pressure and the crossover pressure of MEK was lower than that of n-hexane. In both cases, the crossover pressure increased with an increase in concentration. Also, the activated carbon fiber loaded with toluene and MEK was regenerated by supercritical CO2 in the range of 0.69−0.90 g/cm3. Desorption became favorable with an increase in pressure, and there was an optimal temperature at every pressure condition. However, the regeneration efficiency increased with temperature at the same density of supercritical CO2. In the case of the MEK/toluene mixture, the difference in the desorption rate and desorption amount between two adsorbates was decreased as the pressure was increased. A one-parameter mathematical model assuming linear desorption kinetics matched the experimental data using an activated carbon fiber.

The adsorption equilibria of toluene and gasoline vapors on activated carbon were measured by a static volumetric method. The equilibrium experiments were conducted at (298.15, 318.15, 338.15, 358.15, and 378.15) K and pressures up to 3.1 kPa for toluene and 8.0 kPa for gasoline. The experimental data obtained were correlated by the UNILAN and Sips models, which are generally used for microporous adsorbents such as activated carbon. The Henry constant was calculated to characterize interactions between adsorptive and adsorbent.

The adsorption equilibria of toluene and gasoline vapors on DAY zeolite were measured by a static volumetric method. The equilibrium experiments were conducted at (298.15, 318.15, 338.15, 358.15, and 378.15) K and pressures up to 2.5 kPa for toluene and 7.8 kPa for gasoline. The experimental data obtained were correlated by the Toth and UNILAN models, which are generally used for microporous adsorbents such as zeolite.

The adsorption equilibria of water vapor on activated carbon and DAY zeolite were measured by a static volumetric method. The equilibrium experiments were conducted at (293, 313, 333, 353, and 373) K and pressures up to 3.4 kPa for activated carbon and 1.9 kPa for DAY zeolite. According to the classification of isotherms, the experimental data are correlated by the Dubinin−Serpinsky and Sips models for activated carbon as well as the Toth, UNILAN, and Sips models for DAY zeolite.