The Flow of Liquids in Surface Grooves

We have obtained detailed capillary kinetic data for flow of a series of alcohols with various surface tension to viscosity ratios, γ/μ, spreading in open V-shaped grooves cut in Cu with three different groove angles. The location of the three-phase contact line, z, with time always follows the form...

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Veröffentlicht in:Langmuir 1996-01, Vol.12 (2), p.555-565
Hauptverfasser: Rye, R. R, Mann, J. A, Yost, F. G
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Mann, J. A
Yost, F. G
description We have obtained detailed capillary kinetic data for flow of a series of alcohols with various surface tension to viscosity ratios, γ/μ, spreading in open V-shaped grooves cut in Cu with three different groove angles. The location of the three-phase contact line, z, with time always follows the formula z 2 = K(α,θ)[γh 0/μ]t where α is related to the included groove angle β (α = 90 − β/2), θ is the contact angle, and h 0 is the groove depth. Two theoretical models which assume Poiseuille flow and static advancing contact angles were tested against the experimental data. One is a detailed hydrodynamic model with the basic driving force resulting from the pressure drop across a curved interface. The second depends on the total interfacial energy change, independent of the shape of the liquid interface. Both agree with the experimental data. In agreement with experiment, both models predict that the rate approaches zero as α → θ, and both require α − θ > 0. Both, including a physically unrealistic approximation by a cylindrical capillary, correctly scale the experimental data. Both predict numerical values in general agreement with experiment and with each other. Differentiation between the models is possible only in the K(α,θ) term which is shown to be only weakly dependent on the range of α,θ values studied. In the threshold region where the transition occurs between filled and empty regions of the groove, the liquid height decreases linearly with distance, within experimental limitations, and forms an angle which roughly scales as the contact angle for a significant fraction of the threshold region. On the basis of the present detailed experimental data for both kinetics and threshold profile, the differences between experiment and theory and between the theoretical models are insufficient to allow a clear choice between the models.
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R ; Mann, J. A ; Yost, F. G</creator><creatorcontrib>Rye, R. R ; Mann, J. A ; Yost, F. G ; Sandia National Laboratory</creatorcontrib><description>We have obtained detailed capillary kinetic data for flow of a series of alcohols with various surface tension to viscosity ratios, γ/μ, spreading in open V-shaped grooves cut in Cu with three different groove angles. The location of the three-phase contact line, z, with time always follows the formula z 2 = K(α,θ)[γh 0/μ]t where α is related to the included groove angle β (α = 90 − β/2), θ is the contact angle, and h 0 is the groove depth. Two theoretical models which assume Poiseuille flow and static advancing contact angles were tested against the experimental data. One is a detailed hydrodynamic model with the basic driving force resulting from the pressure drop across a curved interface. The second depends on the total interfacial energy change, independent of the shape of the liquid interface. Both agree with the experimental data. In agreement with experiment, both models predict that the rate approaches zero as α → θ, and both require α − θ &gt; 0. Both, including a physically unrealistic approximation by a cylindrical capillary, correctly scale the experimental data. Both predict numerical values in general agreement with experiment and with each other. Differentiation between the models is possible only in the K(α,θ) term which is shown to be only weakly dependent on the range of α,θ values studied. In the threshold region where the transition occurs between filled and empty regions of the groove, the liquid height decreases linearly with distance, within experimental limitations, and forms an angle which roughly scales as the contact angle for a significant fraction of the threshold region. On the basis of the present detailed experimental data for both kinetics and threshold profile, the differences between experiment and theory and between the theoretical models are insufficient to allow a clear choice between the models.</description><identifier>ISSN: 0743-7463</identifier><identifier>EISSN: 1520-5827</identifier><identifier>DOI: 10.1021/la9500989</identifier><identifier>CODEN: LANGD5</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>40 CHEMISTRY ; ALCOHOLS ; CAPILLARY FLOW ; Chemistry ; ENGINEERING NOT INCLUDED IN OTHER CATEGORIES ; Exact sciences and technology ; FLUID FLOW ; General and physical chemistry ; INTERFACES ; MATHEMATICAL MODELS ; MATHEMATICS, COMPUTERS, INFORMATION SCIENCE, MANAGEMENT, LAW, MISCELLANEOUS ; Solid-liquid interface ; SURFACE ENERGY ; Surface physical chemistry ; SURFACE TENSION ; VISCOSITY</subject><ispartof>Langmuir, 1996-01, Vol.12 (2), p.555-565</ispartof><rights>Copyright © 1996 American Chemical Society</rights><rights>1996 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a350t-6b2e335cc7981cd12a2eb91ae3e65edbc22d81dbbb996c921c2d61e5ecfe80503</citedby><cites>FETCH-LOGICAL-a350t-6b2e335cc7981cd12a2eb91ae3e65edbc22d81dbbb996c921c2d61e5ecfe80503</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/la9500989$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/la9500989$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,885,2765,27076,27924,27925,56738,56788</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=2984385$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/199397$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Rye, R. R</creatorcontrib><creatorcontrib>Mann, J. A</creatorcontrib><creatorcontrib>Yost, F. G</creatorcontrib><creatorcontrib>Sandia National Laboratory</creatorcontrib><title>The Flow of Liquids in Surface Grooves</title><title>Langmuir</title><addtitle>Langmuir</addtitle><description>We have obtained detailed capillary kinetic data for flow of a series of alcohols with various surface tension to viscosity ratios, γ/μ, spreading in open V-shaped grooves cut in Cu with three different groove angles. The location of the three-phase contact line, z, with time always follows the formula z 2 = K(α,θ)[γh 0/μ]t where α is related to the included groove angle β (α = 90 − β/2), θ is the contact angle, and h 0 is the groove depth. Two theoretical models which assume Poiseuille flow and static advancing contact angles were tested against the experimental data. One is a detailed hydrodynamic model with the basic driving force resulting from the pressure drop across a curved interface. The second depends on the total interfacial energy change, independent of the shape of the liquid interface. Both agree with the experimental data. In agreement with experiment, both models predict that the rate approaches zero as α → θ, and both require α − θ &gt; 0. Both, including a physically unrealistic approximation by a cylindrical capillary, correctly scale the experimental data. Both predict numerical values in general agreement with experiment and with each other. Differentiation between the models is possible only in the K(α,θ) term which is shown to be only weakly dependent on the range of α,θ values studied. In the threshold region where the transition occurs between filled and empty regions of the groove, the liquid height decreases linearly with distance, within experimental limitations, and forms an angle which roughly scales as the contact angle for a significant fraction of the threshold region. On the basis of the present detailed experimental data for both kinetics and threshold profile, the differences between experiment and theory and between the theoretical models are insufficient to allow a clear choice between the models.</description><subject>40 CHEMISTRY</subject><subject>ALCOHOLS</subject><subject>CAPILLARY FLOW</subject><subject>Chemistry</subject><subject>ENGINEERING NOT INCLUDED IN OTHER CATEGORIES</subject><subject>Exact sciences and technology</subject><subject>FLUID FLOW</subject><subject>General and physical chemistry</subject><subject>INTERFACES</subject><subject>MATHEMATICAL MODELS</subject><subject>MATHEMATICS, COMPUTERS, INFORMATION SCIENCE, MANAGEMENT, LAW, MISCELLANEOUS</subject><subject>Solid-liquid interface</subject><subject>SURFACE ENERGY</subject><subject>Surface physical chemistry</subject><subject>SURFACE TENSION</subject><subject>VISCOSITY</subject><issn>0743-7463</issn><issn>1520-5827</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1996</creationdate><recordtype>article</recordtype><recordid>eNpt0E1Lw0AQBuBFFKzVg_8gggoeovuRTbJHKbYqtSqteFw2kwldjdm6m_rx741EevI0h3neGXgJOWT0nFHOLmqjJKUqV1tkwCSnscx5tk0GNEtEnCWp2CV7IbzQzohEDcjpYonRuHafkauiqX1f2zJEtonma18ZwGjinfvAsE92KlMHPPibQ_I0vlqMruPp_eRmdDmNjZC0jdOCoxASIFM5g5Jxw7FQzKDAVGJZAOdlzsqiKJRKQXEGvEwZSoQKcyqpGJKj_q4LrdUBbIuwBNc0CK1mSgmVdeasN-BdCB4rvfL2zfhvzaj-LUFvSujscW9XJoCpK28asGET4CpPRC47FvfMhha_NmvjX3WaiUzqxcNcJ4-zZHL7fKdnnT_pvYGgX9zaN10p_7z_AVLhdOA</recordid><startdate>19960124</startdate><enddate>19960124</enddate><creator>Rye, R. 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G</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a350t-6b2e335cc7981cd12a2eb91ae3e65edbc22d81dbbb996c921c2d61e5ecfe80503</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1996</creationdate><topic>40 CHEMISTRY</topic><topic>ALCOHOLS</topic><topic>CAPILLARY FLOW</topic><topic>Chemistry</topic><topic>ENGINEERING NOT INCLUDED IN OTHER CATEGORIES</topic><topic>Exact sciences and technology</topic><topic>FLUID FLOW</topic><topic>General and physical chemistry</topic><topic>INTERFACES</topic><topic>MATHEMATICAL MODELS</topic><topic>MATHEMATICS, COMPUTERS, INFORMATION SCIENCE, MANAGEMENT, LAW, MISCELLANEOUS</topic><topic>Solid-liquid interface</topic><topic>SURFACE ENERGY</topic><topic>Surface physical chemistry</topic><topic>SURFACE TENSION</topic><topic>VISCOSITY</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Rye, R. R</creatorcontrib><creatorcontrib>Mann, J. A</creatorcontrib><creatorcontrib>Yost, F. G</creatorcontrib><creatorcontrib>Sandia National Laboratory</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>OSTI.GOV</collection><jtitle>Langmuir</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Rye, R. R</au><au>Mann, J. A</au><au>Yost, F. G</au><aucorp>Sandia National Laboratory</aucorp><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>The Flow of Liquids in Surface Grooves</atitle><jtitle>Langmuir</jtitle><addtitle>Langmuir</addtitle><date>1996-01-24</date><risdate>1996</risdate><volume>12</volume><issue>2</issue><spage>555</spage><epage>565</epage><pages>555-565</pages><issn>0743-7463</issn><eissn>1520-5827</eissn><coden>LANGD5</coden><abstract>We have obtained detailed capillary kinetic data for flow of a series of alcohols with various surface tension to viscosity ratios, γ/μ, spreading in open V-shaped grooves cut in Cu with three different groove angles. The location of the three-phase contact line, z, with time always follows the formula z 2 = K(α,θ)[γh 0/μ]t where α is related to the included groove angle β (α = 90 − β/2), θ is the contact angle, and h 0 is the groove depth. Two theoretical models which assume Poiseuille flow and static advancing contact angles were tested against the experimental data. One is a detailed hydrodynamic model with the basic driving force resulting from the pressure drop across a curved interface. The second depends on the total interfacial energy change, independent of the shape of the liquid interface. Both agree with the experimental data. In agreement with experiment, both models predict that the rate approaches zero as α → θ, and both require α − θ &gt; 0. Both, including a physically unrealistic approximation by a cylindrical capillary, correctly scale the experimental data. Both predict numerical values in general agreement with experiment and with each other. Differentiation between the models is possible only in the K(α,θ) term which is shown to be only weakly dependent on the range of α,θ values studied. In the threshold region where the transition occurs between filled and empty regions of the groove, the liquid height decreases linearly with distance, within experimental limitations, and forms an angle which roughly scales as the contact angle for a significant fraction of the threshold region. On the basis of the present detailed experimental data for both kinetics and threshold profile, the differences between experiment and theory and between the theoretical models are insufficient to allow a clear choice between the models.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/la9500989</doi><tpages>11</tpages></addata></record>
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source American Chemical Society Journals
subjects 40 CHEMISTRY
ALCOHOLS
CAPILLARY FLOW
Chemistry
ENGINEERING NOT INCLUDED IN OTHER CATEGORIES
Exact sciences and technology
FLUID FLOW
General and physical chemistry
INTERFACES
MATHEMATICAL MODELS
MATHEMATICS, COMPUTERS, INFORMATION SCIENCE, MANAGEMENT, LAW, MISCELLANEOUS
Solid-liquid interface
SURFACE ENERGY
Surface physical chemistry
SURFACE TENSION
VISCOSITY
title The Flow of Liquids in Surface Grooves
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