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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Main Authors: Lucas Sandoli Lima, Carlos Eduardo Keutenedjian Mady
Format: Article
Language:English
Published: MDPI AG 2021-03-01
Series:Entropy
Subjects:
Online Access:https://www.mdpi.com/1099-4300/23/4/415
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spelling 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
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AT carloseduardokeutenedjianmady energyandexergyanalysisofanabsorptionandmechanicalsystemforadehumidificationunitinagelatinfactory
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