Transient heat and moisture transfer characteristics of a liquid-to-air membrane energy exchanger (LAMEE) model verification and extrapolation

2013 ◽  
Vol 66 ◽  
pp. 757-771 ◽  
Author(s):  
Ramin Namvar ◽  
Gaoming Ge ◽  
Carey J. Simonson ◽  
Robert W. Besant
Keyword(s):  
Moisture Transfer ◽  
Model Verification ◽  
Heat And Moisture Transfer ◽  
Transfer Characteristics ◽  
Membrane Energy ◽  
Heat And Moisture

scholarly journals Dehumidification performance investigation of run-around membrane energy exchanger system

2016 ◽  
Vol 20 (6) ◽  
pp. 1927-1938 ◽  
Author(s):  
Miklos Kassai ◽  
Gaoming Ge ◽  
Carey Simonson
Keyword(s):  
Salt Solution ◽  
Moisture Transfer ◽  
Heat And Moisture Transfer ◽  
Solution Flow ◽  
Permeable Membrane ◽  
Air Temperatures ◽  
Air Stream ◽  
Membrane Energy ◽  
Air Conditioning Systems ◽  
Heat And Moisture

Liquid-to-air membrane energy exchanger is a novel membrane base energy exchanger, which allows both heat and moisture transfer between air and a salt solution. It uses semi-permeable membrane to eliminate entrainment of liquid desiccant as aerosols in air stream and allow simultaneous heat and moisture transfer between salt solution flow and airflow. The heat and mass transfer performance of a single liquid-to-air membrane energy exchanger is significantly dependent on two dimensionless parameters. They are the number of heat transfer units (NTU) and the ratio of heat capacity rates between solution flow and air flow (Cr*). The liquid-to-air membrane energy exchangers can also be applied in a run-around membrane energy exchanger system, which is mainly comprised of two liquid-to-air membrane energy exchangers and a closed loop of aqueous desiccant solution and used as a passive energy recovery system to recover the energy (both heat and moisture) from the exhaust air to precondition the supply air in air conditioning systems. In this study the dehumidification capacity of a run-around membrane energy exchanger is investigated numerically at different exhaust air temperatures and Cr* values. Increasing the exhaust air temperature or the Cr* would enhance the dehumidification capacity of the a run-around membrane energy exchanger system under Cr*?1, but the improvement is limited. The dehumidification capacity at low Cr* is much lower than that under the optimal Cr* value (Cr*=3.2) where the maximum latent effectiveness is obtained.

Sign in / Sign up

Export Citation Format

Share Document