Two-phase frictional pressure drop measurements in U-type wavy tubes subject to horizontal and vertical arrangements
Two-phase frictional pressure gradient is significantly affected by the flow patterns. Though most of the U-type wavy tubes are commonly vertically installed in the air-conditioning and refrigerating systems, yet none investigations had reported the two-phase frictional pressure loss in vertical U-t...
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Veröffentlicht in: | Applied thermal engineering 2008-06, Vol.28 (8), p.847-855 |
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description | Two-phase frictional pressure gradient is significantly affected by the flow patterns. Though most of the U-type wavy tubes are commonly vertically installed in the air-conditioning and refrigerating systems, yet none investigations had reported the two-phase frictional pressure loss in vertical U-type wavy tubes. This study presents the measurements of R-134a two-phase frictional pressure gradient subject to vertical and horizontal arrangements of a U-type wavy tube with inner diameter of 5.07
mm and a curvature ratio of 5. The ratio between two-phase pressure gradients of U-bend and straight tube is about 2.5–3.5. For the straight tube, the frictional two-phase pressure gradient ratio between the vertical and horizontal arrangements is marginally higher (1.0–1.2) for annular flow pattern at
x
>
0.5, and is 1.0–1.4 for the U-bend in the wavy tube. The higher resistance in the vertical arrangement is due to the buoyancy force against the flow inertia. However, for
x
<
0.5, this ratio is gradually increased due to the difference of flow pattern. The ratio is increased to 1.8
in the straight tube. For the U-bend, the ratio is 2.1 for flow entering the upper tube and is 1.5 for flow entering the lower tube at
x
=
0.1 and
G
=
200
kg/m
2
s. For the vertical wavy tube, additional effects like the flow pattern transition, liquid flow reversal, and freezing slug may cause additional pressure drops. |
doi_str_mv | 10.1016/j.applthermaleng.2007.07.012 |
format | Article |
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mm and a curvature ratio of 5. The ratio between two-phase pressure gradients of U-bend and straight tube is about 2.5–3.5. For the straight tube, the frictional two-phase pressure gradient ratio between the vertical and horizontal arrangements is marginally higher (1.0–1.2) for annular flow pattern at
x
>
0.5, and is 1.0–1.4 for the U-bend in the wavy tube. The higher resistance in the vertical arrangement is due to the buoyancy force against the flow inertia. However, for
x
<
0.5, this ratio is gradually increased due to the difference of flow pattern. The ratio is increased to 1.8
in the straight tube. For the U-bend, the ratio is 2.1 for flow entering the upper tube and is 1.5 for flow entering the lower tube at
x
=
0.1 and
G
=
200
kg/m
2
s. For the vertical wavy tube, additional effects like the flow pattern transition, liquid flow reversal, and freezing slug may cause additional pressure drops.</description><identifier>ISSN: 1359-4311</identifier><identifier>DOI: 10.1016/j.applthermaleng.2007.07.012</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Air conditioning. Ventilation ; Applied sciences ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Friction factor ; Heat transfer ; Heating, air conditioning and ventilation ; Techniques, equipment. Control. Metering ; Theoretical studies. Data and constants. Metering ; Two-phase frictional pressure gradient ; U-type wavy tube</subject><ispartof>Applied thermal engineering, 2008-06, Vol.28 (8), p.847-855</ispartof><rights>2007 Elsevier Ltd</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c391t-4133f85a50fccf1ab099344b08e3ce8e8606a13ba25f0bb024a50db59de1a95f3</citedby><cites>FETCH-LOGICAL-c391t-4133f85a50fccf1ab099344b08e3ce8e8606a13ba25f0bb024a50db59de1a95f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.applthermaleng.2007.07.012$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=20166973$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Chen, Ing Youn</creatorcontrib><creatorcontrib>Wu, Yu-Shi</creatorcontrib><creatorcontrib>Liaw, Jane-Sunn</creatorcontrib><creatorcontrib>Wang, Chi-Chuan</creatorcontrib><title>Two-phase frictional pressure drop measurements in U-type wavy tubes subject to horizontal and vertical arrangements</title><title>Applied thermal engineering</title><description>Two-phase frictional pressure gradient is significantly affected by the flow patterns. Though most of the U-type wavy tubes are commonly vertically installed in the air-conditioning and refrigerating systems, yet none investigations had reported the two-phase frictional pressure loss in vertical U-type wavy tubes. This study presents the measurements of R-134a two-phase frictional pressure gradient subject to vertical and horizontal arrangements of a U-type wavy tube with inner diameter of 5.07
mm and a curvature ratio of 5. The ratio between two-phase pressure gradients of U-bend and straight tube is about 2.5–3.5. For the straight tube, the frictional two-phase pressure gradient ratio between the vertical and horizontal arrangements is marginally higher (1.0–1.2) for annular flow pattern at
x
>
0.5, and is 1.0–1.4 for the U-bend in the wavy tube. The higher resistance in the vertical arrangement is due to the buoyancy force against the flow inertia. However, for
x
<
0.5, this ratio is gradually increased due to the difference of flow pattern. The ratio is increased to 1.8
in the straight tube. For the U-bend, the ratio is 2.1 for flow entering the upper tube and is 1.5 for flow entering the lower tube at
x
=
0.1 and
G
=
200
kg/m
2
s. For the vertical wavy tube, additional effects like the flow pattern transition, liquid flow reversal, and freezing slug may cause additional pressure drops.</description><subject>Air conditioning. Ventilation</subject><subject>Applied sciences</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Friction factor</subject><subject>Heat transfer</subject><subject>Heating, air conditioning and ventilation</subject><subject>Techniques, equipment. Control. Metering</subject><subject>Theoretical studies. Data and constants. Metering</subject><subject>Two-phase frictional pressure gradient</subject><subject>U-type wavy tube</subject><issn>1359-4311</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNqNkEFr3DAQhXVoIekm_0GHNjdvJcvetSGXEJK0EMglOYuxPMpqsSVXI2_Y_vrIbCj0FnggZnj6hvcY-y7FWgq5-blfwzQNaYdxhAH967oUYrteJMsv7Fyqui0qJeUZ-0a0F3nbbKtzlp7fQjHtgJDb6ExywcPAp4hEc0TexzDxEWEZRvSJuPP8pUjHCfkbHI48zR0Sp7nbo0k8Bb4L0f0NPmUK-J4fMCZnliFG8K8nyAX7amEgvPx4V-zl_u759lfx-PTw-_bmsTCqlamopFK2qaEW1hgroRNtq6qqEw0qgw02G7EBqTooayu6TpRVtvZd3fYooa2tWrGrE3eK4c-MlPToyOAwgMcwk1bltqxV1opdn4wmBqKIVk_RjRCPWgq91Kv3-v969VKvXiTL_P3Hxx2gnNXmpMbRP0aZAZt2q7Lv_uTDHPrgMGoyDr3B3sVcn-6D-9zBd9dWnwM</recordid><startdate>20080601</startdate><enddate>20080601</enddate><creator>Chen, Ing Youn</creator><creator>Wu, Yu-Shi</creator><creator>Liaw, Jane-Sunn</creator><creator>Wang, Chi-Chuan</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>20080601</creationdate><title>Two-phase frictional pressure drop measurements in U-type wavy tubes subject to horizontal and vertical arrangements</title><author>Chen, Ing Youn ; Wu, Yu-Shi ; Liaw, Jane-Sunn ; Wang, Chi-Chuan</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c391t-4133f85a50fccf1ab099344b08e3ce8e8606a13ba25f0bb024a50db59de1a95f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>Air conditioning. Ventilation</topic><topic>Applied sciences</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Friction factor</topic><topic>Heat transfer</topic><topic>Heating, air conditioning and ventilation</topic><topic>Techniques, equipment. Control. Metering</topic><topic>Theoretical studies. Data and constants. Metering</topic><topic>Two-phase frictional pressure gradient</topic><topic>U-type wavy tube</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Chen, Ing Youn</creatorcontrib><creatorcontrib>Wu, Yu-Shi</creatorcontrib><creatorcontrib>Liaw, Jane-Sunn</creatorcontrib><creatorcontrib>Wang, Chi-Chuan</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Applied thermal engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Chen, Ing Youn</au><au>Wu, Yu-Shi</au><au>Liaw, Jane-Sunn</au><au>Wang, Chi-Chuan</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Two-phase frictional pressure drop measurements in U-type wavy tubes subject to horizontal and vertical arrangements</atitle><jtitle>Applied thermal engineering</jtitle><date>2008-06-01</date><risdate>2008</risdate><volume>28</volume><issue>8</issue><spage>847</spage><epage>855</epage><pages>847-855</pages><issn>1359-4311</issn><abstract>Two-phase frictional pressure gradient is significantly affected by the flow patterns. Though most of the U-type wavy tubes are commonly vertically installed in the air-conditioning and refrigerating systems, yet none investigations had reported the two-phase frictional pressure loss in vertical U-type wavy tubes. This study presents the measurements of R-134a two-phase frictional pressure gradient subject to vertical and horizontal arrangements of a U-type wavy tube with inner diameter of 5.07
mm and a curvature ratio of 5. The ratio between two-phase pressure gradients of U-bend and straight tube is about 2.5–3.5. For the straight tube, the frictional two-phase pressure gradient ratio between the vertical and horizontal arrangements is marginally higher (1.0–1.2) for annular flow pattern at
x
>
0.5, and is 1.0–1.4 for the U-bend in the wavy tube. The higher resistance in the vertical arrangement is due to the buoyancy force against the flow inertia. However, for
x
<
0.5, this ratio is gradually increased due to the difference of flow pattern. The ratio is increased to 1.8
in the straight tube. For the U-bend, the ratio is 2.1 for flow entering the upper tube and is 1.5 for flow entering the lower tube at
x
=
0.1 and
G
=
200
kg/m
2
s. For the vertical wavy tube, additional effects like the flow pattern transition, liquid flow reversal, and freezing slug may cause additional pressure drops.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.applthermaleng.2007.07.012</doi><tpages>9</tpages></addata></record> |
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subjects | Air conditioning. Ventilation Applied sciences Energy Energy. Thermal use of fuels Exact sciences and technology Friction factor Heat transfer Heating, air conditioning and ventilation Techniques, equipment. Control. Metering Theoretical studies. Data and constants. Metering Two-phase frictional pressure gradient U-type wavy tube |
title | Two-phase frictional pressure drop measurements in U-type wavy tubes subject to horizontal and vertical arrangements |
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