Abstract

With rising insulation standards, the use of mechanical ventilation, especially in non-residential buildings, is becoming increasingly relevant. To ensure thermal comfort and avoid health problems for people in the room, cost- and energy-intensive humidification of the supply air is necessary. The use of moisture recovery systems can thus significantly reduce the energy consumption of ventilation systems. Despite this energy-saving potential, moisture recovery systems are rarely used in ventilation systems. To forecast the efficiency of moisture recovery systems in partial load operation and under different climatic conditions, a dynamic model of a membrane-based enthalpy exchanger was developed in the object-oriented modelling language Modelica. The model is based on the solution diffusion model, a quite common approach. In contrast to the models found in the literature, the sorption process is not assumed to be in equilibrium state. Rather, as a first approach the membrane’s permeance, consisting of the solubility and diffusion coefficient, is modelled with a linear dependency on the moisture difference between the two incoming airflows. A parameter fitting has been carried out with experimental data to determine the unknown material parameters. The model containing the fitted parameter set was validated using different experimental data.

Highlights

  • Maintaining the thermal comfort in non-residential buildings is the task of Heating, Ventilation and Air Conditioning (HVAC) systems

  • We examined the enthalpy exchanger for different temperature and humidity differences between the two incoming airflows

  • We investigated the influence of different volume flow rates through the enthalpy exchanger

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Summary

Introduction

Maintaining the thermal comfort in non-residential buildings is the task of Heating, Ventilation and Air Conditioning (HVAC) systems. To heating and cooling processes the air humidification and dehumidification is necessary to provide comfortable air conditions in a certain building. On contrary to other researches, the author does not model the sorption process directly, but uses an overall membrane permeance As this permeance is as constant, the model does not provide any dependence on the moisture difference between exhaust and supply air. A dynamic model of a membrane-based enthalpy exchanger is developed using the solution diffusion model and a membrane’s permeance with a linear dependency on the moisture difference between the two incoming airflows

Membrane-based Enthalpy Exchanger
Modelling
Modelling of heat and moisture transfer
Modelling approach for membrane’s permeance
Modelling the cross-flow portion
Parameter Fitting
Comparison of experimental data with simulation results
Conclusion and outlook
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