Experimental performance of membrane water absorption in LiBr solution with and without cooling

•Adiabatic and cooled absorption are tested in a membrane microchannel absorber.•LiBr-water adiabatic absorption can operate without the need of a cooling tower.•Adiabatic/cooled behaviour agrees with simulations when varying mass flow rate.•Measured pressure drop is acceptable for the LiBr-water ab...

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Veröffentlicht in:Applied thermal engineering 2020-11, Vol.180, p.115786, Article 115786
Hauptverfasser: de Vega, M., García-Hernando, N., Venegas, M.
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container_title Applied thermal engineering
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creator de Vega, M.
García-Hernando, N.
Venegas, M.
description •Adiabatic and cooled absorption are tested in a membrane microchannel absorber.•LiBr-water adiabatic absorption can operate without the need of a cooling tower.•Adiabatic/cooled behaviour agrees with simulations when varying mass flow rate.•Measured pressure drop is acceptable for the LiBr-water absorption requirements. The operation of a microchannel membrane-based absorber using LiBr-water as absorbent-refrigerant pair is presented. The absorber is a stainless-steel plate structure, provided with microchannels coupled with a membrane which separates the water vapor and the solution. The same device is experimentally tested in two modes of operation. In one, water is used to cool the absorption process (as occurs in conventional absorbers) circulating through channels separated from the solution by a thin plate. In the second mode, no water circulates, and the absorption is adiabatic. The absorption rates obtained using both configurations are compared, evaluating the influence of the solution mass flux. The absorption ratio (absorbed vapor to solution mass flow rate) is studied as a function of the cooling water temperature and its effect on solution temperature and pressure potential. The mass transfer coefficient is inferred from the measurements. Also, the measured pressure drop along the channels shows the viability for the operation of this type of absorber.
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The operation of a microchannel membrane-based absorber using LiBr-water as absorbent-refrigerant pair is presented. The absorber is a stainless-steel plate structure, provided with microchannels coupled with a membrane which separates the water vapor and the solution. The same device is experimentally tested in two modes of operation. In one, water is used to cool the absorption process (as occurs in conventional absorbers) circulating through channels separated from the solution by a thin plate. In the second mode, no water circulates, and the absorption is adiabatic. The absorption rates obtained using both configurations are compared, evaluating the influence of the solution mass flux. The absorption ratio (absorbed vapor to solution mass flow rate) is studied as a function of the cooling water temperature and its effect on solution temperature and pressure potential. The mass transfer coefficient is inferred from the measurements. 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The operation of a microchannel membrane-based absorber using LiBr-water as absorbent-refrigerant pair is presented. The absorber is a stainless-steel plate structure, provided with microchannels coupled with a membrane which separates the water vapor and the solution. The same device is experimentally tested in two modes of operation. In one, water is used to cool the absorption process (as occurs in conventional absorbers) circulating through channels separated from the solution by a thin plate. In the second mode, no water circulates, and the absorption is adiabatic. The absorption rates obtained using both configurations are compared, evaluating the influence of the solution mass flux. The absorption ratio (absorbed vapor to solution mass flow rate) is studied as a function of the cooling water temperature and its effect on solution temperature and pressure potential. The mass transfer coefficient is inferred from the measurements. 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The operation of a microchannel membrane-based absorber using LiBr-water as absorbent-refrigerant pair is presented. The absorber is a stainless-steel plate structure, provided with microchannels coupled with a membrane which separates the water vapor and the solution. The same device is experimentally tested in two modes of operation. In one, water is used to cool the absorption process (as occurs in conventional absorbers) circulating through channels separated from the solution by a thin plate. In the second mode, no water circulates, and the absorption is adiabatic. The absorption rates obtained using both configurations are compared, evaluating the influence of the solution mass flux. The absorption ratio (absorbed vapor to solution mass flow rate) is studied as a function of the cooling water temperature and its effect on solution temperature and pressure potential. The mass transfer coefficient is inferred from the measurements. 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subjects Absorbers
Absorption systems
Adsorption
Cooling
Cooling rate
Flat sheet membrane
Heat transfer
Mass flow rate
Mass transfer
Membranes
Microchannel-absorber
Microchannels
Pressure
Pressure drop
Stainless steels
Steel plates
Temperature
Thin plates
Water
Water absorption
Water temperature
Water vapor
Water–lithium bromide mixture
title Experimental performance of membrane water absorption in LiBr solution with and without cooling
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