Heat and Mass Transfer in the Adsorbent Bed of an Adsorption Heat Pump

Abstract

The heat and mass transfer equations governing an adsorbent bed in an adsorption heat pump and the mass balance equation for the adsorbent particles in the adsorbent bed were solved numerically to simulate the cycle of a basic adsorption heat pump, which includes isobaric adsorption, isosteric heating, isobaric desorption, and isosteric cooling processes. The finite difference method was used to solve the set of governing equations, which are highly nonlinear and coupled. The pressures of the evaporator and condenser were 2 and 20 kPa, respectively, and the regeneration temperature of the bed was 403 K. Changes in the temperature, adsorptive pressure, and adsorbate concentration in the adsorbent bed at different steps of the cycle were determined. The basic simulated cycle is presented in a ClausiusClapeyron diagram, which illustrates the changes in average pressure and temperature of the adsorbent bed throughout the cycle. The results of the simulation indicated that the most time-consuming processes in the adsorption heat pump cycle were isobaric adsorption and isobaric desorption. The high thermal resistance of the bed slows down heat transfer, prolonging adsorption and desorption processes.

Modeling and Simulation of Combined Heat and Mass Transfer in Zeolite SAPO‐34 Coating for an Adsorption Heat Pump

“…Freni [24]. Despite many advantages of the adsorption cooling machine, heat and mass transfers inside the adsorbent bed are considered poor; consequently, they can cause low system performance [5,25,26]. In order to overcome these issues, the coated heat bed, for adsorption cooling systems, showed very promising properties and better performances in terms of specific cooling power (SCP) [27].…”