Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle

Recently, a CaCl2-BaCl2-NH3 chemisorption freezing cycle driven by a low-temperature heat source has drawn an increasing amount of attention. To develop a working pair with a more desirable performance than CaCl2-BaCl2-NH3, working pairs of CaCl2-NaBr-NH3, SrCl2-BaCl2-NH3, and SrCl2-NH4Cl-NH3 were i...

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Main Authors: Jiang Long, Lu Huitong, Wang Ruzhu, Wang Liwei
Format: Article
Language:zho
Published: Journal of Refrigeration Magazines Agency Co., Ltd. 2017-01-01
Series:Zhileng xuebao
Subjects:
Online Access:http://www.zhilengxuebao.com/thesisDetails#10.3969/j.issn.0253-4339.2017.06.007
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author Jiang Long
Lu Huitong
Wang Ruzhu
Wang Liwei
author_facet Jiang Long
Lu Huitong
Wang Ruzhu
Wang Liwei
author_sort Jiang Long
collection DOAJ
description Recently, a CaCl2-BaCl2-NH3 chemisorption freezing cycle driven by a low-temperature heat source has drawn an increasing amount of attention. To develop a working pair with a more desirable performance than CaCl2-BaCl2-NH3, working pairs of CaCl2-NaBr-NH3, SrCl2-BaCl2-NH3, and SrCl2-NH4Cl-NH3 were investigated and compared. Most composite adsorbents were developed with a novel matrix of expanded natural graphite treated with sulfuric acid (ENG-TSA), leaving one serial with expanded natural graphite (ENG) for comparison. For SrCl2-NH4Cl-NH3 and CaCl2-NaBr-NH3, experimental results show that the maximum adsorption quantities are 95.4% and 88.6% of the theoretical values, respectively. Simulation results indicate that the best results are obtained from CaCl2-NaBr-NH3, and its specific cooling power (SCP) and coefficient of performance (COP) are as high as 260.74 W/kg and 0.285, respectively, which are 15.1% and 5.6% better than the values for CaCl2-BaCl2-NH3. It is also noted that, for different working pairs, the COP, cooling capacity, and SCP range from 0.215 to 0.285, 2 to 3.65 kW, and 161.4 to 260.74 W/kg, respectively. Comparisons also show that the ENG-TSA matrix effectively improves the SCP. For example, the SCP of CaCl2-BaCl2-NH3 is improved by 40.2%, when compared with a working pair with the ENG matrix.
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spelling doaj-art-387d4f879b3748abb83e36f6d89f7f9a2025-08-20T02:02:58ZzhoJournal of Refrigeration Magazines Agency Co., Ltd.Zhileng xuebao0253-43392017-01-013866513314Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration CycleJiang LongLu HuitongWang RuzhuWang LiweiRecently, a CaCl2-BaCl2-NH3 chemisorption freezing cycle driven by a low-temperature heat source has drawn an increasing amount of attention. To develop a working pair with a more desirable performance than CaCl2-BaCl2-NH3, working pairs of CaCl2-NaBr-NH3, SrCl2-BaCl2-NH3, and SrCl2-NH4Cl-NH3 were investigated and compared. Most composite adsorbents were developed with a novel matrix of expanded natural graphite treated with sulfuric acid (ENG-TSA), leaving one serial with expanded natural graphite (ENG) for comparison. For SrCl2-NH4Cl-NH3 and CaCl2-NaBr-NH3, experimental results show that the maximum adsorption quantities are 95.4% and 88.6% of the theoretical values, respectively. Simulation results indicate that the best results are obtained from CaCl2-NaBr-NH3, and its specific cooling power (SCP) and coefficient of performance (COP) are as high as 260.74 W/kg and 0.285, respectively, which are 15.1% and 5.6% better than the values for CaCl2-BaCl2-NH3. It is also noted that, for different working pairs, the COP, cooling capacity, and SCP range from 0.215 to 0.285, 2 to 3.65 kW, and 161.4 to 260.74 W/kg, respectively. Comparisons also show that the ENG-TSA matrix effectively improves the SCP. For example, the SCP of CaCl2-BaCl2-NH3 is improved by 40.2%, when compared with a working pair with the ENG matrix.http://www.zhilengxuebao.com/thesisDetails#10.3969/j.issn.0253-4339.2017.06.007sorptionrefrigeration cycleworking pairsENG-TSA
spellingShingle Jiang Long
Lu Huitong
Wang Ruzhu
Wang Liwei
Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle
Zhileng xuebao
sorption
refrigeration cycle
working pairs
ENG-TSA
title Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle
title_full Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle
title_fullStr Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle
title_full_unstemmed Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle
title_short Experimental Investigation on Working Pairs for a Two-stage Sorption Refrigeration Cycle
title_sort experimental investigation on working pairs for a two stage sorption refrigeration cycle
topic sorption
refrigeration cycle
working pairs
ENG-TSA
url http://www.zhilengxuebao.com/thesisDetails#10.3969/j.issn.0253-4339.2017.06.007
work_keys_str_mv AT jianglong experimentalinvestigationonworkingpairsforatwostagesorptionrefrigerationcycle
AT luhuitong experimentalinvestigationonworkingpairsforatwostagesorptionrefrigerationcycle
AT wangruzhu experimentalinvestigationonworkingpairsforatwostagesorptionrefrigerationcycle
AT wangliwei experimentalinvestigationonworkingpairsforatwostagesorptionrefrigerationcycle