This article introduces a tentative to modify an adsorption inverse cycle adopting a membrane separation technology instead of the vaporization separation technology present into a classic absorption refrigerator cycle. The proposed approach consists is in the use of a membrane technology in order to separate the two fluids (refrigerant and absorbent), instead of a separation by distillation. In practice, the cycle is modified by inserting a hydrophobic Membrane Contactor in order to make a liquid-liquid extraction of a solute easily absorbed in water (solvent). In this way, the classical absorption cycle can be modified with the substantial reduction of heat supply at elevated temperature, used to separate the solute from solvent, replacing it with the pump work necessary to pressurize and circulate the fluids involved in the cycle. The latter is enabled because the separation of the two fluids in the Contactor Membrane is obtained thanks to a generation of a concentration gradient. The adopted membrane contactor, commercially available, is realized by means of hollow porous fiber of polypropylene (PP) positioned in a cartridge of polyethylene (PE). So, concentration gradient is realized between the two size of the membrane, i.e. water at high concentration of the solute and the other size in which an organic solvent flows at low concentration of the solute. As secondary fluid, organic solvent, we adopted and tested diesel oil. The result demonstrates the technical feasibility of the proposed cycle through some preliminary results obtained adopting ethylic alcohol and acetaldehyde, both of them absorbed by water.

Membrane Separation Technology Applied in a Refrigeration Cycle

E. Nino
;
R. Di Tommaso
2019-01-01

Abstract

This article introduces a tentative to modify an adsorption inverse cycle adopting a membrane separation technology instead of the vaporization separation technology present into a classic absorption refrigerator cycle. The proposed approach consists is in the use of a membrane technology in order to separate the two fluids (refrigerant and absorbent), instead of a separation by distillation. In practice, the cycle is modified by inserting a hydrophobic Membrane Contactor in order to make a liquid-liquid extraction of a solute easily absorbed in water (solvent). In this way, the classical absorption cycle can be modified with the substantial reduction of heat supply at elevated temperature, used to separate the solute from solvent, replacing it with the pump work necessary to pressurize and circulate the fluids involved in the cycle. The latter is enabled because the separation of the two fluids in the Contactor Membrane is obtained thanks to a generation of a concentration gradient. The adopted membrane contactor, commercially available, is realized by means of hollow porous fiber of polypropylene (PP) positioned in a cartridge of polyethylene (PE). So, concentration gradient is realized between the two size of the membrane, i.e. water at high concentration of the solute and the other size in which an organic solvent flows at low concentration of the solute. As secondary fluid, organic solvent, we adopted and tested diesel oil. The result demonstrates the technical feasibility of the proposed cycle through some preliminary results obtained adopting ethylic alcohol and acetaldehyde, both of them absorbed by water.
2019
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11563/143010
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