Experimental Performance of a Membrane Desorber with a H2O/LiCl Mixture for Absorption Chiller Applications
For absorption cooling cycles using water as a refrigerant, H2O/LiCl mixtures are suitable for replacing conventional H2O/LiBr mixtures. In addition, membrane devices can be used to develop compact and lighter absorption systems, and they can operate with H2O/LiCl mixtures. The present paper describ...
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Published in | Membranes (Basel) Vol. 12; no. 12; p. 1184 |
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Language | English |
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Abstract | For absorption cooling cycles using water as a refrigerant, H2O/LiCl mixtures are suitable for replacing conventional H2O/LiBr mixtures. In addition, membrane devices can be used to develop compact and lighter absorption systems, and they can operate with H2O/LiCl mixtures. The present paper describes an experimental evaluation of a membrane desorber/condenser operating at atmospheric pressure. Two operation modes were analyzed: continuous cycle operation and intermittent operation. For the first operation mode, the maximum desorption rate was 3.49 kg/h·m2, with a solution temperature of 90.3 °C and a condensation temperature of 25.1 °C. The lowest desorption rate value was 0.26 kg/h·m2, with a solution temperature of 75.4 °C and a condensation temperature of 40.1 °C. In the second mode, after three operating hours, the refrigerant fluid produced, per 1 m2 of membrane area, 7.7, 5.6, 4.3, and 2.2 kg, at solution temperatures of 90.3, 85.3, 80.4, and 75.4 °C, respectively. A one-dimension heat and mass transfer model is presented. The calculated values of desorption rate and outlet temperatures were compared with the experimental data; a square correlation coefficient of 0.9929 was reached for the desorption rate; meanwhile, for the outlet solution temperatures and the outlet cooling-water temperatures, a square correlation coefficient up to 0.9991 was achieved. The membrane desorber has the advantages of operating at atmospheric-pressure conditions, high condensation temperature, the ability to use different saline solution working mixtures, and different operation methods. These advantages can lead to new absorption systems. |
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AbstractList | For absorption cooling cycles using water as a refrigerant, H2O/LiCl mixtures are suitable for replacing conventional H2O/LiBr mixtures. In addition, membrane devices can be used to develop compact and lighter absorption systems, and they can operate with H2O/LiCl mixtures. The present paper describes an experimental evaluation of a membrane desorber/condenser operating at atmospheric pressure. Two operation modes were analyzed: continuous cycle operation and intermittent operation. For the first operation mode, the maximum desorption rate was 3.49 kg/h·m2, with a solution temperature of 90.3 °C and a condensation temperature of 25.1 °C. The lowest desorption rate value was 0.26 kg/h·m2, with a solution temperature of 75.4 °C and a condensation temperature of 40.1 °C. In the second mode, after three operating hours, the refrigerant fluid produced, per 1 m2 of membrane area, 7.7, 5.6, 4.3, and 2.2 kg, at solution temperatures of 90.3, 85.3, 80.4, and 75.4 °C, respectively. A one-dimension heat and mass transfer model is presented. The calculated values of desorption rate and outlet temperatures were compared with the experimental data; a square correlation coefficient of 0.9929 was reached for the desorption rate; meanwhile, for the outlet solution temperatures and the outlet cooling-water temperatures, a square correlation coefficient up to 0.9991 was achieved. The membrane desorber has the advantages of operating at atmospheric-pressure conditions, high condensation temperature, the ability to use different saline solution working mixtures, and different operation methods. These advantages can lead to new absorption systems. For absorption cooling cycles using water as a refrigerant, H 2 O/LiCl mixtures are suitable for replacing conventional H 2 O/LiBr mixtures. In addition, membrane devices can be used to develop compact and lighter absorption systems, and they can operate with H 2 O/LiCl mixtures. The present paper describes an experimental evaluation of a membrane desorber/condenser operating at atmospheric pressure. Two operation modes were analyzed: continuous cycle operation and intermittent operation. For the first operation mode, the maximum desorption rate was 3.49 kg/h·m 2 , with a solution temperature of 90.3 °C and a condensation temperature of 25.1 °C. The lowest desorption rate value was 0.26 kg/h·m 2 , with a solution temperature of 75.4 °C and a condensation temperature of 40.1 °C. In the second mode, after three operating hours, the refrigerant fluid produced, per 1 m 2 of membrane area, 7.7, 5.6, 4.3, and 2.2 kg, at solution temperatures of 90.3, 85.3, 80.4, and 75.4 °C, respectively. A one-dimension heat and mass transfer model is presented. The calculated values of desorption rate and outlet temperatures were compared with the experimental data; a square correlation coefficient of 0.9929 was reached for the desorption rate; meanwhile, for the outlet solution temperatures and the outlet cooling-water temperatures, a square correlation coefficient up to 0.9991 was achieved. The membrane desorber has the advantages of operating at atmospheric-pressure conditions, high condensation temperature, the ability to use different saline solution working mixtures, and different operation methods. These advantages can lead to new absorption systems. |
Author | Rivera, Wilfrido Medina-Caballero, Iván Leonardo Galindo-Luna, Yuridiana Rocio Ibarra-Bahena, Jonathan Dehesa-Carrasco, Ulises |
AuthorAffiliation | 2 Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana-Iztapalapa, Mexico City 09340, Mexico 1 Subcoordinación de Conservación de Cuencas y Servicios Ambientales, Instituto Mexicano de Tecnología del Agua, Jiutepec 62550, Mexico 3 Instituto de Energías Renovables, Universidad Nacional Autónoma de México, Temixco 62580, Mexico |
AuthorAffiliation_xml | – name: 1 Subcoordinación de Conservación de Cuencas y Servicios Ambientales, Instituto Mexicano de Tecnología del Agua, Jiutepec 62550, Mexico – name: 2 Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana-Iztapalapa, Mexico City 09340, Mexico – name: 3 Instituto de Energías Renovables, Universidad Nacional Autónoma de México, Temixco 62580, Mexico |
Author_xml | – sequence: 1 givenname: Jonathan orcidid: 0000-0002-2574-0895 surname: Ibarra-Bahena fullname: Ibarra-Bahena, Jonathan – sequence: 2 givenname: Ulises surname: Dehesa-Carrasco fullname: Dehesa-Carrasco, Ulises – sequence: 3 givenname: Yuridiana Rocio surname: Galindo-Luna fullname: Galindo-Luna, Yuridiana Rocio – sequence: 4 givenname: Iván Leonardo surname: Medina-Caballero fullname: Medina-Caballero, Iván Leonardo – sequence: 5 givenname: Wilfrido orcidid: 0000-0002-9845-5542 surname: Rivera fullname: Rivera, Wilfrido |
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CitedBy_id | crossref_primary_10_1016_j_applthermaleng_2024_122574 crossref_primary_10_1016_j_tsep_2024_102399 |
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Snippet | For absorption cooling cycles using water as a refrigerant, H2O/LiCl mixtures are suitable for replacing conventional H2O/LiBr mixtures. In addition, membrane... For absorption cooling cycles using water as a refrigerant, H 2 O/LiCl mixtures are suitable for replacing conventional H 2 O/LiBr mixtures. In addition,... |
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SubjectTerms | Absorption absorption chiller Absorption cooling Condensation Condensers Cooling Correlation coefficient Correlation coefficients Desorption Efficiency Heat exchangers LiCl mixture Lithium chloride Mass transfer membrane distillation Membranes Mixtures Refrigerants Saline solutions Simulation Water temperature |
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Title | Experimental Performance of a Membrane Desorber with a H2O/LiCl Mixture for Absorption Chiller Applications |
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