Performance Of Adsorption Heat Pump Research Articles

Influence of desorption temperature on the thermodynamic performance of adsorption heat pump

In the paper an analysis of the desorption temperature effect on the thermodynamic efficiency of the adsorption heat pumps is presented. The thermodynamic performance of heat pump is determined by Coefficient of Performance (COP) as well as exergetic efficiency coefficient (ηex) at the adsorption equilibrium conditions and compared to the performance at heat of evaporation of the working fluid conditions. Possible estimation of reduced efficiency of adsorption silica gel/water heat pump, as distinct from the equilibrium efficiency in realistic technical system is presented.

Pore structure and water adsorptivity of petroleum coke-derived activated carbon for adsorption heat pump–Influence of hydrogen content of coke

Abstract In order to achieve high cooling output performance of adsorption heat pump (AHP) by improving water adsorptivity of an adsorbent, we have been developing activated carbon (AC) prepared from petroleum coke with potassium hydroxide chemical activation. In particular, this research dealt with the effect of hydrogen content of coke on pore structure, surface chemistry and water vapor adsorptivity of AC prepared. Three petroleum cokes with H/C molar ratios ranging from 0.266 to 0.417 were employed as a raw carbonaceous material, and activated at 773 K for 1 h under various weight ratios of KOH/coke, R . Pore structure, such as BET surface area and pore size distribution, was estimated by N 2 and CO 2 adsorption isotherms. Amount of adsorbed water vapor on AC was measured by a volumetric gas adsorption apparatus. The total content of acidic surface functional groups was determined by the Boehm titration method. As a result, it was found that development of pores was promoted at higher hydrogen content and higher KOH/coke weight ratio. Further, the pores were mainly consisted of micropore. Concerning water vapor adsorption, the same trend as N 2 adsorption could be observed; i.e. amount of water adsorbed on AC increased as increasing H/C molar ratio of coke. In the operation relative pressure range of AHP ranging from 0.11 to 0.38, the adsorptivity of water vapor on AC prepared from coke with H/C = 0.417 at R = 5 achieved about 1.2 times higher than that of commercial silica gel, which is 0.19 kg/kg of water adsorptivity. It was also suggested that a steep increase in water adsorptivity at relative pressure over 0.2 was attributed to a well-developed micropore greater than 0.5 nm and high hydrophilicity of activated carbon prepared.