Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory
In this paper, an energy and exergy analysis is applied to the air dehumidification unit of a liquid desiccant system in an industrial gelatin conveyor dryer. The working fluid is a binary solution of lithium chloride (LiCl) in water. Dry air is used in order to decrease the amount of liquid in the...
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doaj-12957cd7956e4dd690ff6b5409dab1122021-03-31T23:03:04ZengMDPI AGEntropy1099-43002021-03-012341541510.3390/e23040415Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin FactoryLucas Sandoli Lima0Carlos Eduardo Keutenedjian Mady1School of Mechanical Engineering, University of Campinas, Mendeleyev St., 200—Cidade Universitária, Campinas 13083-970, BrazilDepartment of Mechanical Engineering, Centro Universitário da FEI, São Bernardo do Campo 09850-901, BrazilIn this paper, an energy and exergy analysis is applied to the air dehumidification unit of a liquid desiccant system in an industrial gelatin conveyor dryer. The working fluid is a binary solution of lithium chloride (LiCl) in water. Dry air is used in order to decrease the amount of liquid in the gelatin. Therefore, the environmental air must have its absolute humidity reduced from about 12 g/kg to the project target, which is 5 g/kg. The process is a cycle using an absorption desiccant unit (LiCl in water), where the weak solution absorbs water vapor from the air. In the regenerator, condensation of the solution (desorption) from the moist air occurs. As a result, the steam consumption of the desorber and electrical power used for the vapor compression chiller (with ammonia, NH<inline-formula><math display="inline"><semantics><msub><mrow></mrow><mn>3</mn></msub></semantics></math></inline-formula>, as working fluid) are the primary sources of cost for the factory. To improve the plant’s energy and exergy behaviors, the process is evaluated using a mathematical model of the system processes. In addition, we evaluate the substitution of the vapor compression chiller by an absorption unit (lithium bromide (LiBr) in water). The performance indicators of the compression vapor systems showed the best results. Even when using the condenser’s energy to pre-heat the solution, the installed system proved to be more effective.https://www.mdpi.com/1099-4300/23/4/415absorption unitair dehumidificationdesiccant systemexergy analysis |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Lucas Sandoli Lima Carlos Eduardo Keutenedjian Mady |
spellingShingle |
Lucas Sandoli Lima Carlos Eduardo Keutenedjian Mady Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory Entropy absorption unit air dehumidification desiccant system exergy analysis |
author_facet |
Lucas Sandoli Lima Carlos Eduardo Keutenedjian Mady |
author_sort |
Lucas Sandoli Lima |
title |
Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory |
title_short |
Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory |
title_full |
Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory |
title_fullStr |
Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory |
title_full_unstemmed |
Energy and Exergy Analysis of an Absorption and Mechanical System for a Dehumidification Unit in a Gelatin Factory |
title_sort |
energy and exergy analysis of an absorption and mechanical system for a dehumidification unit in a gelatin factory |
publisher |
MDPI AG |
series |
Entropy |
issn |
1099-4300 |
publishDate |
2021-03-01 |
description |
In this paper, an energy and exergy analysis is applied to the air dehumidification unit of a liquid desiccant system in an industrial gelatin conveyor dryer. The working fluid is a binary solution of lithium chloride (LiCl) in water. Dry air is used in order to decrease the amount of liquid in the gelatin. Therefore, the environmental air must have its absolute humidity reduced from about 12 g/kg to the project target, which is 5 g/kg. The process is a cycle using an absorption desiccant unit (LiCl in water), where the weak solution absorbs water vapor from the air. In the regenerator, condensation of the solution (desorption) from the moist air occurs. As a result, the steam consumption of the desorber and electrical power used for the vapor compression chiller (with ammonia, NH<inline-formula><math display="inline"><semantics><msub><mrow></mrow><mn>3</mn></msub></semantics></math></inline-formula>, as working fluid) are the primary sources of cost for the factory. To improve the plant’s energy and exergy behaviors, the process is evaluated using a mathematical model of the system processes. In addition, we evaluate the substitution of the vapor compression chiller by an absorption unit (lithium bromide (LiBr) in water). The performance indicators of the compression vapor systems showed the best results. Even when using the condenser’s energy to pre-heat the solution, the installed system proved to be more effective. |
topic |
absorption unit air dehumidification desiccant system exergy analysis |
url |
https://www.mdpi.com/1099-4300/23/4/415 |
work_keys_str_mv |
AT lucassandolilima energyandexergyanalysisofanabsorptionandmechanicalsystemforadehumidificationunitinagelatinfactory AT carloseduardokeutenedjianmady energyandexergyanalysisofanabsorptionandmechanicalsystemforadehumidificationunitinagelatinfactory |
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