Loading…
Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems
A recently built experimental setup was employed for the estimation of the solid−liquid equilibria of alternative refrigerant systems. The behavior of two binaries, i.e., carbon dioxide + 1,1-difluoroethane (CO2 + R152a) and nitrous oxide + 1,1-difluoroethane (N2O + R152a), was measured down to temp...
Saved in:
Published in: | Journal of chemical and engineering data 2007-11, Vol.52 (6), p.2451-2454 |
---|---|
Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Online Access: | Get full text |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
cited_by | |
---|---|
cites | |
container_end_page | 2454 |
container_issue | 6 |
container_start_page | 2451 |
container_title | Journal of chemical and engineering data |
container_volume | 52 |
creator | Di Nicola, Giovanni Giuliani, Giuliano Polonara, Fabio Santori, Giulio Stryjek, Roman |
description | A recently built experimental setup was employed for the estimation of the solid−liquid equilibria of alternative refrigerant systems. The behavior of two binaries, i.e., carbon dioxide + 1,1-difluoroethane (CO2 + R152a) and nitrous oxide + 1,1-difluoroethane (N2O + R152a), was measured down to temperatures of 132 K. The triple points of CO2 and N2O were measured to confirm the reliability of the apparatus. The triple point of R152a was also measured; however, the pressure at the triple point for this fluid was too low to accurately measure with the current apparatus. All triple-point data measured revealed a generally good consistency with the literature. The results obtained for the mixtures were interpreted by means of the Schröder equation. |
doi_str_mv | 10.1021/je700384e |
format | article |
fullrecord | <record><control><sourceid>acs_pasca</sourceid><recordid>TN_cdi_pascalfrancis_primary_19862943</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>a768519525</sourcerecordid><originalsourceid>FETCH-LOGICAL-a218t-17eb6f8cf0e3b4e5eecdcc98ebf5722370e7df67a2ce22d512c3a0558769818d3</originalsourceid><addsrcrecordid>eNpFkM1KAzEUhYMoWKsL3yAbVzKan8kks5RSqzhYsaO4C3fyg6nTH5MW7Bu49hF9EkcqdXMvl3P4uOcgdErJBSWMXk6dJISr3O2hHhWMZILyfB_1SCdmpSjUITpKaUoIySWjPTScLNpgvz-_qvC-DhYPu9mGJgbAfhHx6tXhwZjhc_zY0QDD3OJ7Nt7dk01auVk6Rgce2uRO_nYfPV0P68FNVo1Ht4OrKgNG1Sqj0jWFV8YTx5vcCeeMNaZUrvFCMsYlcdL6QgIzjjErKDMciBBKFqWiyvI-Ottyl5AMtD7C3ISklzHMIG40LVXBypx3vmzrC917Hzsd4psuJJdC1w8TzZ_ru5dSSJ3_c8EkPV2s47xLoSnRv53qXaf8BxvmZWg</addsrcrecordid><sourcetype>Index Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems</title><source>American Chemical Society:Jisc Collections:American Chemical Society Read & Publish Agreement 2022-2024 (Reading list)</source><creator>Di Nicola, Giovanni ; Giuliani, Giuliano ; Polonara, Fabio ; Santori, Giulio ; Stryjek, Roman</creator><creatorcontrib>Di Nicola, Giovanni ; Giuliani, Giuliano ; Polonara, Fabio ; Santori, Giulio ; Stryjek, Roman</creatorcontrib><description>A recently built experimental setup was employed for the estimation of the solid−liquid equilibria of alternative refrigerant systems. The behavior of two binaries, i.e., carbon dioxide + 1,1-difluoroethane (CO2 + R152a) and nitrous oxide + 1,1-difluoroethane (N2O + R152a), was measured down to temperatures of 132 K. The triple points of CO2 and N2O were measured to confirm the reliability of the apparatus. The triple point of R152a was also measured; however, the pressure at the triple point for this fluid was too low to accurately measure with the current apparatus. All triple-point data measured revealed a generally good consistency with the literature. The results obtained for the mixtures were interpreted by means of the Schröder equation.</description><identifier>ISSN: 0021-9568</identifier><identifier>EISSN: 1520-5134</identifier><identifier>DOI: 10.1021/je700384e</identifier><identifier>CODEN: JCEAAX</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Applied sciences ; Chemistry ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; General and physical chemistry ; Liquid-solid equilibria ; Phase equilibria ; Refrigerants ; Refrigerating engineering ; Refrigerating engineering. Cryogenics. Food conservation</subject><ispartof>Journal of chemical and engineering data, 2007-11, Vol.52 (6), p.2451-2454</ispartof><rights>Copyright © 2007 American Chemical Society</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27923,27924</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=19862943$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Di Nicola, Giovanni</creatorcontrib><creatorcontrib>Giuliani, Giuliano</creatorcontrib><creatorcontrib>Polonara, Fabio</creatorcontrib><creatorcontrib>Santori, Giulio</creatorcontrib><creatorcontrib>Stryjek, Roman</creatorcontrib><title>Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems</title><title>Journal of chemical and engineering data</title><addtitle>J. Chem. Eng. Data</addtitle><description>A recently built experimental setup was employed for the estimation of the solid−liquid equilibria of alternative refrigerant systems. The behavior of two binaries, i.e., carbon dioxide + 1,1-difluoroethane (CO2 + R152a) and nitrous oxide + 1,1-difluoroethane (N2O + R152a), was measured down to temperatures of 132 K. The triple points of CO2 and N2O were measured to confirm the reliability of the apparatus. The triple point of R152a was also measured; however, the pressure at the triple point for this fluid was too low to accurately measure with the current apparatus. All triple-point data measured revealed a generally good consistency with the literature. The results obtained for the mixtures were interpreted by means of the Schröder equation.</description><subject>Applied sciences</subject><subject>Chemistry</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>Liquid-solid equilibria</subject><subject>Phase equilibria</subject><subject>Refrigerants</subject><subject>Refrigerating engineering</subject><subject>Refrigerating engineering. Cryogenics. Food conservation</subject><issn>0021-9568</issn><issn>1520-5134</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNpFkM1KAzEUhYMoWKsL3yAbVzKan8kks5RSqzhYsaO4C3fyg6nTH5MW7Bu49hF9EkcqdXMvl3P4uOcgdErJBSWMXk6dJISr3O2hHhWMZILyfB_1SCdmpSjUITpKaUoIySWjPTScLNpgvz-_qvC-DhYPu9mGJgbAfhHx6tXhwZjhc_zY0QDD3OJ7Nt7dk01auVk6Rgce2uRO_nYfPV0P68FNVo1Ht4OrKgNG1Sqj0jWFV8YTx5vcCeeMNaZUrvFCMsYlcdL6QgIzjjErKDMciBBKFqWiyvI-Ottyl5AMtD7C3ISklzHMIG40LVXBypx3vmzrC917Hzsd4psuJJdC1w8TzZ_ru5dSSJ3_c8EkPV2s47xLoSnRv53qXaf8BxvmZWg</recordid><startdate>20071115</startdate><enddate>20071115</enddate><creator>Di Nicola, Giovanni</creator><creator>Giuliani, Giuliano</creator><creator>Polonara, Fabio</creator><creator>Santori, Giulio</creator><creator>Stryjek, Roman</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope></search><sort><creationdate>20071115</creationdate><title>Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems</title><author>Di Nicola, Giovanni ; Giuliani, Giuliano ; Polonara, Fabio ; Santori, Giulio ; Stryjek, Roman</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a218t-17eb6f8cf0e3b4e5eecdcc98ebf5722370e7df67a2ce22d512c3a0558769818d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Applied sciences</topic><topic>Chemistry</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>General and physical chemistry</topic><topic>Liquid-solid equilibria</topic><topic>Phase equilibria</topic><topic>Refrigerants</topic><topic>Refrigerating engineering</topic><topic>Refrigerating engineering. Cryogenics. Food conservation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Di Nicola, Giovanni</creatorcontrib><creatorcontrib>Giuliani, Giuliano</creatorcontrib><creatorcontrib>Polonara, Fabio</creatorcontrib><creatorcontrib>Santori, Giulio</creatorcontrib><creatorcontrib>Stryjek, Roman</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><jtitle>Journal of chemical and engineering data</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Di Nicola, Giovanni</au><au>Giuliani, Giuliano</au><au>Polonara, Fabio</au><au>Santori, Giulio</au><au>Stryjek, Roman</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems</atitle><jtitle>Journal of chemical and engineering data</jtitle><addtitle>J. Chem. Eng. Data</addtitle><date>2007-11-15</date><risdate>2007</risdate><volume>52</volume><issue>6</issue><spage>2451</spage><epage>2454</epage><pages>2451-2454</pages><issn>0021-9568</issn><eissn>1520-5134</eissn><coden>JCEAAX</coden><abstract>A recently built experimental setup was employed for the estimation of the solid−liquid equilibria of alternative refrigerant systems. The behavior of two binaries, i.e., carbon dioxide + 1,1-difluoroethane (CO2 + R152a) and nitrous oxide + 1,1-difluoroethane (N2O + R152a), was measured down to temperatures of 132 K. The triple points of CO2 and N2O were measured to confirm the reliability of the apparatus. The triple point of R152a was also measured; however, the pressure at the triple point for this fluid was too low to accurately measure with the current apparatus. All triple-point data measured revealed a generally good consistency with the literature. The results obtained for the mixtures were interpreted by means of the Schröder equation.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/je700384e</doi><tpages>4</tpages><oa>free_for_read</oa></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0021-9568 |
ispartof | Journal of chemical and engineering data, 2007-11, Vol.52 (6), p.2451-2454 |
issn | 0021-9568 1520-5134 |
language | eng |
recordid | cdi_pascalfrancis_primary_19862943 |
source | American Chemical Society:Jisc Collections:American Chemical Society Read & Publish Agreement 2022-2024 (Reading list) |
subjects | Applied sciences Chemistry Energy Energy. Thermal use of fuels Exact sciences and technology General and physical chemistry Liquid-solid equilibria Phase equilibria Refrigerants Refrigerating engineering Refrigerating engineering. Cryogenics. Food conservation |
title | Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems |
url | http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-12T04%3A23%3A11IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-acs_pasca&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Solid%E2%88%92Liquid%20Equilibria%20for%20the%20CO2%20+%20R152a%20and%20N2O%20+%20R152a%20Systems&rft.jtitle=Journal%20of%20chemical%20and%20engineering%20data&rft.au=Di%20Nicola,%20Giovanni&rft.date=2007-11-15&rft.volume=52&rft.issue=6&rft.spage=2451&rft.epage=2454&rft.pages=2451-2454&rft.issn=0021-9568&rft.eissn=1520-5134&rft.coden=JCEAAX&rft_id=info:doi/10.1021/je700384e&rft_dat=%3Cacs_pasca%3Ea768519525%3C/acs_pasca%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-a218t-17eb6f8cf0e3b4e5eecdcc98ebf5722370e7df67a2ce22d512c3a0558769818d3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true |