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Heat transfer coefficients for propane (R-290), isobutane (R-600a), and 50/50 mixture of propane and isobutane
Tube-side heat transfer coefficients for single-phase flow, evaporation, and condensation are presented for propane (R-290), isobutane (R-600a), and a 50/50 mixture (by weight) of propane and isobutane. Heat transfer coefficients have been presented for smooth tubes. The correlations for evaporation...
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description | Tube-side heat transfer coefficients for single-phase flow, evaporation, and condensation are presented for propane (R-290), isobutane (R-600a), and a 50/50 mixture (by weight) of propane and isobutane. Heat transfer coefficients have been presented for smooth tubes. The correlations for evaporation and condensation have previously been verified for R-12 and other refrigerants. The mass flux of the refrigerant is varied over a wide range that is typically encountered in residential, commercial, and automotive applications. The REFPROP computer program has been used to determine the thermodynamic properties for R-290, R-600a, and R-290 /R-600a. This study shows that the heat transfer coefficients for hydrocarbons are significantly higher than hose for both R-12 and R-134a. A summary of the heat transfer coefficient enhancement of the hydrocarbons in comparison to both R-12 and R-134a is presented in tables. |
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Heat transfer coefficients have been presented for smooth tubes. The correlations for evaporation and condensation have previously been verified for R-12 and other refrigerants. The mass flux of the refrigerant is varied over a wide range that is typically encountered in residential, commercial, and automotive applications. The REFPROP computer program has been used to determine the thermodynamic properties for R-290, R-600a, and R-290 /R-600a. This study shows that the heat transfer coefficients for hydrocarbons are significantly higher than hose for both R-12 and R-134a. A summary of the heat transfer coefficient enhancement of the hydrocarbons in comparison to both R-12 and R-134a is presented in tables.</description><identifier>ISSN: 0001-2505</identifier><identifier>CODEN: ASHTAG</identifier><language>eng</language><publisher>Atlanta: American Society of Heating, Refrigeration and Air Conditioning Engineers, Inc</publisher><subject>2-METHYLPROPANE ; AIR CONDITIONERS ; AUTOMOBILES ; BINARY MIXTURES ; Butane ; Condensation ; CORRELATIONS ; ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION ; EVAPORATION ; Flow of fluids ; HEAT TRANSFER ; MATERIAL SUBSTITUTION ; PROPANE ; REFRIGERANTS ; REFRIGERATING MACHINERY ; Thermal effects ; VAPOR CONDENSATION</subject><ispartof>ASHRAE transactions, 1998, Vol.104 (2), p.1159-1172</ispartof><rights>Copyright American Society of Heating, Refrigeration and Air Conditioning Engineers, Inc. 1998</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,309,310,314,780,784,789,790,885,4024,4050,4051,23930,23931,25140</link.rule.ids><backlink>$$Uhttps://www.osti.gov/biblio/687676$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Mathur, Gursaran D</creatorcontrib><title>Heat transfer coefficients for propane (R-290), isobutane (R-600a), and 50/50 mixture of propane and isobutane</title><title>ASHRAE transactions</title><description>Tube-side heat transfer coefficients for single-phase flow, evaporation, and condensation are presented for propane (R-290), isobutane (R-600a), and a 50/50 mixture (by weight) of propane and isobutane. Heat transfer coefficients have been presented for smooth tubes. The correlations for evaporation and condensation have previously been verified for R-12 and other refrigerants. The mass flux of the refrigerant is varied over a wide range that is typically encountered in residential, commercial, and automotive applications. The REFPROP computer program has been used to determine the thermodynamic properties for R-290, R-600a, and R-290 /R-600a. This study shows that the heat transfer coefficients for hydrocarbons are significantly higher than hose for both R-12 and R-134a. A summary of the heat transfer coefficient enhancement of the hydrocarbons in comparison to both R-12 and R-134a is presented in tables.</description><subject>2-METHYLPROPANE</subject><subject>AIR CONDITIONERS</subject><subject>AUTOMOBILES</subject><subject>BINARY MIXTURES</subject><subject>Butane</subject><subject>Condensation</subject><subject>CORRELATIONS</subject><subject>ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION</subject><subject>EVAPORATION</subject><subject>Flow of fluids</subject><subject>HEAT TRANSFER</subject><subject>MATERIAL SUBSTITUTION</subject><subject>PROPANE</subject><subject>REFRIGERANTS</subject><subject>REFRIGERATING MACHINERY</subject><subject>Thermal effects</subject><subject>VAPOR 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D</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-o153t-517ec9165e41d9721c1723a7bf6c378cbf37f85678c6ab73cd7f3f226077c0d33</frbrgroupid><rsrctype>conference_proceedings</rsrctype><prefilter>conference_proceedings</prefilter><language>eng</language><creationdate>1998</creationdate><topic>2-METHYLPROPANE</topic><topic>AIR CONDITIONERS</topic><topic>AUTOMOBILES</topic><topic>BINARY MIXTURES</topic><topic>Butane</topic><topic>Condensation</topic><topic>CORRELATIONS</topic><topic>ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION</topic><topic>EVAPORATION</topic><topic>Flow of fluids</topic><topic>HEAT TRANSFER</topic><topic>MATERIAL SUBSTITUTION</topic><topic>PROPANE</topic><topic>REFRIGERANTS</topic><topic>REFRIGERATING MACHINERY</topic><topic>Thermal effects</topic><topic>VAPOR CONDENSATION</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mathur, Gursaran D</creatorcontrib><collection>ProQuest Central 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(R-600a), and 50/50 mixture of propane and isobutane</atitle><btitle>ASHRAE transactions</btitle><date>1998</date><risdate>1998</risdate><volume>104</volume><issue>2</issue><spage>1159</spage><epage>1172</epage><pages>1159-1172</pages><issn>0001-2505</issn><coden>ASHTAG</coden><abstract>Tube-side heat transfer coefficients for single-phase flow, evaporation, and condensation are presented for propane (R-290), isobutane (R-600a), and a 50/50 mixture (by weight) of propane and isobutane. Heat transfer coefficients have been presented for smooth tubes. The correlations for evaporation and condensation have previously been verified for R-12 and other refrigerants. The mass flux of the refrigerant is varied over a wide range that is typically encountered in residential, commercial, and automotive applications. The REFPROP computer program has been used to determine the thermodynamic properties for R-290, R-600a, and R-290 /R-600a. This study shows that the heat transfer coefficients for hydrocarbons are significantly higher than hose for both R-12 and R-134a. A summary of the heat transfer coefficient enhancement of the hydrocarbons in comparison to both R-12 and R-134a is presented in tables.</abstract><cop>Atlanta</cop><pub>American Society of Heating, Refrigeration and Air Conditioning Engineers, Inc</pub><tpages>14</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0001-2505 |
ispartof | ASHRAE transactions, 1998, Vol.104 (2), p.1159-1172 |
issn | 0001-2505 |
language | eng |
recordid | cdi_osti_scitechconnect_687676 |
source | ASHRAE Publications |
subjects | 2-METHYLPROPANE AIR CONDITIONERS AUTOMOBILES BINARY MIXTURES Butane Condensation CORRELATIONS ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION EVAPORATION Flow of fluids HEAT TRANSFER MATERIAL SUBSTITUTION PROPANE REFRIGERANTS REFRIGERATING MACHINERY Thermal effects VAPOR CONDENSATION |
title | Heat transfer coefficients for propane (R-290), isobutane (R-600a), and 50/50 mixture of propane and isobutane |
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