Control of viscous instability by variation of injection rate in a fluid with time-dependent rheology
Using variational calculus, we investigate the time-dependent injection rate that minimises the growth of the Saffman–Taylor instability when a finite volume of fluid is injected in a finite time, $t_{f}$ , into a Hele-Shaw cell. We first consider a planar interface, and show that, with a constant v...
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description | Using variational calculus, we investigate the time-dependent injection rate that minimises the growth of the Saffman–Taylor instability when a finite volume of fluid is injected in a finite time,
$t_{f}$
, into a Hele-Shaw cell. We first consider a planar interface, and show that, with a constant viscosity ratio, the constant injection rate is optimal. When the viscosity of the displacing fluid,
$\unicode[STIX]{x1D707}_{1}(t)$
, gradually increases over time, as may occur with a slowly gelling polymer solution, the optimal injection rate,
$U^{\ast }(t)$
, involves a gradual increase in the flow rate with time. This leads to a smaller initial value of flow rate than the constant injection rate, finishing with a larger value. Such optimisation can lead to a substantial suppression of the instability as compared to the constant injection case if the characteristic gelling time is comparable to
$t_{f}$
. In contrast, for either relatively slow or fast gelling, there is much less benefit in selecting the optimal injection rate,
$U^{\ast }(t)$
, as compared to the constant injection rate. In the case of a constant injection rate from a point source,
$Q$
, then with a constant viscosity ratio the fastest-growing perturbation on the radially spreading front involves axisymmetric modes whose wavenumber increases with time. Approximating the discrete azimuthal modes by a continuous distribution, we find the injection rate that minimises growth,
$Q^{\ast }(t)$
. We find that there is a critical time for injection,
$t_{f}^{\dagger }$
, such that if
$t_{f}>t_{f}^{\dagger }$
then
$Q^{\ast }(t)$
can be chosen so that the interface is always stable. This critical time emerges from the case with an injection rate given by
$Q^{\ast }\sim t^{-1/3}$
. As the total injection time is reduced to values
$t_{f} |
doi_str_mv | 10.1017/jfm.2017.581 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_journals_1973759472</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><cupid>10_1017_jfm_2017_581</cupid><sourcerecordid>1973759472</sourcerecordid><originalsourceid>FETCH-LOGICAL-c302t-d725acef6b71b35e8b5b2f8b6e27ed35e6b7bab7453d1c435d3397cc206cc223</originalsourceid><addsrcrecordid>eNptkMtOwzAQRS0EEqWw4wMssSXBjyRulqjiJVVi073lV1pHSVxspyh_j0O7YMFmZu7MmRnpAnCPUY4RZk9t0-ckFXm5whdggYuqzlhVlJdggRAhGcYEXYObEFqEMEU1WwCzdkP0roOugUcblBsDtEOIQtrOxgnKCR6FtyJaN8yMHVqjfoUX0SQJBWy60Wr4beMeRtubTJuDGbQZIvR74zq3m27BVSO6YO7OeQm2ry_b9Xu2-Xz7WD9vMkURiZlmpBTKNJVkWNLSrGQpSbOSlSHM6NRIAykkK0qqsSpoqSmtmVIEVSkQugQPp7MH775GEyJv3eiH9JHjmlFW1gWbqccTpbwLwZuGH7zthZ84Rnz2kScf-ewjTz4mPD_jopfe6p35c_W_hR-gfnba</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1973759472</pqid></control><display><type>article</type><title>Control of viscous instability by variation of injection rate in a fluid with time-dependent rheology</title><source>Cambridge University Press Journals Complete</source><creator>Beeson-Jones, Tim H. ; Woods, Andrew W.</creator><creatorcontrib>Beeson-Jones, Tim H. ; Woods, Andrew W.</creatorcontrib><description>Using variational calculus, we investigate the time-dependent injection rate that minimises the growth of the Saffman–Taylor instability when a finite volume of fluid is injected in a finite time,
$t_{f}$
, into a Hele-Shaw cell. We first consider a planar interface, and show that, with a constant viscosity ratio, the constant injection rate is optimal. When the viscosity of the displacing fluid,
$\unicode[STIX]{x1D707}_{1}(t)$
, gradually increases over time, as may occur with a slowly gelling polymer solution, the optimal injection rate,
$U^{\ast }(t)$
, involves a gradual increase in the flow rate with time. This leads to a smaller initial value of flow rate than the constant injection rate, finishing with a larger value. Such optimisation can lead to a substantial suppression of the instability as compared to the constant injection case if the characteristic gelling time is comparable to
$t_{f}$
. In contrast, for either relatively slow or fast gelling, there is much less benefit in selecting the optimal injection rate,
$U^{\ast }(t)$
, as compared to the constant injection rate. In the case of a constant injection rate from a point source,
$Q$
, then with a constant viscosity ratio the fastest-growing perturbation on the radially spreading front involves axisymmetric modes whose wavenumber increases with time. Approximating the discrete azimuthal modes by a continuous distribution, we find the injection rate that minimises growth,
$Q^{\ast }(t)$
. We find that there is a critical time for injection,
$t_{f}^{\dagger }$
, such that if
$t_{f}>t_{f}^{\dagger }$
then
$Q^{\ast }(t)$
can be chosen so that the interface is always stable. This critical time emerges from the case with an injection rate given by
$Q^{\ast }\sim t^{-1/3}$
. As the total injection time is reduced to values
$t_{f}<t_{f}^{\dagger }$
, the system becomes progressively more unstable, and the optimal injection rate for an idealised continuous distribution of azimuthal modes asymptotes to a flow rate that increases linearly with time. As for the one-dimensional case, if the viscosity of the injection fluid gradually increases over time, then the optimal injection rate has a smaller initial value but gradually increases to larger values than for the analogous constant viscosity problem. If the displacing fluid features shear-thinning rheology, then the optimal injection rate involves a smaller flow rate at early times, although not as large a reduction as in the Newtonian case, and a larger flow rate at late times, although not as large an increase as in the Newtonian case.</description><identifier>ISSN: 0022-1120</identifier><identifier>EISSN: 1469-7645</identifier><identifier>DOI: 10.1017/jfm.2017.581</identifier><language>eng</language><publisher>Cambridge, UK: Cambridge University Press</publisher><subject>Asymptotes ; Calculus of variations ; Control stability ; Distribution ; Enhanced oil recovery ; Flow rates ; Flow velocity ; Fluid mechanics ; Fluids ; Gelation ; Injection ; Instability ; Modes ; Polymers ; Rheological properties ; Rheology ; Taylor instability ; Time dependence ; Viscosity ; Viscosity ratio ; Water pollution ; Wavelengths</subject><ispartof>Journal of fluid mechanics, 2017-10, Vol.829, p.214-235</ispartof><rights>2017 Cambridge University Press</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c302t-d725acef6b71b35e8b5b2f8b6e27ed35e6b7bab7453d1c435d3397cc206cc223</citedby><cites>FETCH-LOGICAL-c302t-d725acef6b71b35e8b5b2f8b6e27ed35e6b7bab7453d1c435d3397cc206cc223</cites><orcidid>0000-0002-0253-3260 ; 0000-0002-5098-9940</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.cambridge.org/core/product/identifier/S002211201700581X/type/journal_article$$EHTML$$P50$$Gcambridge$$H</linktohtml><link.rule.ids>164,314,777,781,27905,27906,55609</link.rule.ids></links><search><creatorcontrib>Beeson-Jones, Tim H.</creatorcontrib><creatorcontrib>Woods, Andrew W.</creatorcontrib><title>Control of viscous instability by variation of injection rate in a fluid with time-dependent rheology</title><title>Journal of fluid mechanics</title><addtitle>J. Fluid Mech</addtitle><description>Using variational calculus, we investigate the time-dependent injection rate that minimises the growth of the Saffman–Taylor instability when a finite volume of fluid is injected in a finite time,
$t_{f}$
, into a Hele-Shaw cell. We first consider a planar interface, and show that, with a constant viscosity ratio, the constant injection rate is optimal. When the viscosity of the displacing fluid,
$\unicode[STIX]{x1D707}_{1}(t)$
, gradually increases over time, as may occur with a slowly gelling polymer solution, the optimal injection rate,
$U^{\ast }(t)$
, involves a gradual increase in the flow rate with time. This leads to a smaller initial value of flow rate than the constant injection rate, finishing with a larger value. Such optimisation can lead to a substantial suppression of the instability as compared to the constant injection case if the characteristic gelling time is comparable to
$t_{f}$
. In contrast, for either relatively slow or fast gelling, there is much less benefit in selecting the optimal injection rate,
$U^{\ast }(t)$
, as compared to the constant injection rate. In the case of a constant injection rate from a point source,
$Q$
, then with a constant viscosity ratio the fastest-growing perturbation on the radially spreading front involves axisymmetric modes whose wavenumber increases with time. Approximating the discrete azimuthal modes by a continuous distribution, we find the injection rate that minimises growth,
$Q^{\ast }(t)$
. We find that there is a critical time for injection,
$t_{f}^{\dagger }$
, such that if
$t_{f}>t_{f}^{\dagger }$
then
$Q^{\ast }(t)$
can be chosen so that the interface is always stable. This critical time emerges from the case with an injection rate given by
$Q^{\ast }\sim t^{-1/3}$
. As the total injection time is reduced to values
$t_{f}<t_{f}^{\dagger }$
, the system becomes progressively more unstable, and the optimal injection rate for an idealised continuous distribution of azimuthal modes asymptotes to a flow rate that increases linearly with time. As for the one-dimensional case, if the viscosity of the injection fluid gradually increases over time, then the optimal injection rate has a smaller initial value but gradually increases to larger values than for the analogous constant viscosity problem. If the displacing fluid features shear-thinning rheology, then the optimal injection rate involves a smaller flow rate at early times, although not as large a reduction as in the Newtonian case, and a larger flow rate at late times, although not as large an increase as in the Newtonian case.</description><subject>Asymptotes</subject><subject>Calculus of variations</subject><subject>Control stability</subject><subject>Distribution</subject><subject>Enhanced oil recovery</subject><subject>Flow rates</subject><subject>Flow velocity</subject><subject>Fluid mechanics</subject><subject>Fluids</subject><subject>Gelation</subject><subject>Injection</subject><subject>Instability</subject><subject>Modes</subject><subject>Polymers</subject><subject>Rheological properties</subject><subject>Rheology</subject><subject>Taylor instability</subject><subject>Time dependence</subject><subject>Viscosity</subject><subject>Viscosity ratio</subject><subject>Water pollution</subject><subject>Wavelengths</subject><issn>0022-1120</issn><issn>1469-7645</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><sourceid>8G5</sourceid><sourceid>ABUWG</sourceid><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><sourceid>GNUQQ</sourceid><sourceid>GUQSH</sourceid><sourceid>M2O</sourceid><recordid>eNptkMtOwzAQRS0EEqWw4wMssSXBjyRulqjiJVVi073lV1pHSVxspyh_j0O7YMFmZu7MmRnpAnCPUY4RZk9t0-ckFXm5whdggYuqzlhVlJdggRAhGcYEXYObEFqEMEU1WwCzdkP0roOugUcblBsDtEOIQtrOxgnKCR6FtyJaN8yMHVqjfoUX0SQJBWy60Wr4beMeRtubTJuDGbQZIvR74zq3m27BVSO6YO7OeQm2ry_b9Xu2-Xz7WD9vMkURiZlmpBTKNJVkWNLSrGQpSbOSlSHM6NRIAykkK0qqsSpoqSmtmVIEVSkQugQPp7MH775GEyJv3eiH9JHjmlFW1gWbqccTpbwLwZuGH7zthZ84Rnz2kScf-ewjTz4mPD_jopfe6p35c_W_hR-gfnba</recordid><startdate>20171025</startdate><enddate>20171025</enddate><creator>Beeson-Jones, Tim H.</creator><creator>Woods, Andrew W.</creator><general>Cambridge University Press</general><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>7TB</scope><scope>7U5</scope><scope>7UA</scope><scope>7XB</scope><scope>88I</scope><scope>8FD</scope><scope>8FE</scope><scope>8FG</scope><scope>8FK</scope><scope>8G5</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AEUYN</scope><scope>AFKRA</scope><scope>ARAPS</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>FR3</scope><scope>GNUQQ</scope><scope>GUQSH</scope><scope>H8D</scope><scope>H96</scope><scope>HCIFZ</scope><scope>KR7</scope><scope>L.G</scope><scope>L6V</scope><scope>L7M</scope><scope>M2O</scope><scope>M2P</scope><scope>M7S</scope><scope>MBDVC</scope><scope>P5Z</scope><scope>P62</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope><scope>Q9U</scope><scope>S0W</scope><orcidid>https://orcid.org/0000-0002-0253-3260</orcidid><orcidid>https://orcid.org/0000-0002-5098-9940</orcidid></search><sort><creationdate>20171025</creationdate><title>Control of viscous instability by variation of injection rate in a fluid with time-dependent rheology</title><author>Beeson-Jones, Tim H. ; Woods, Andrew W.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c302t-d725acef6b71b35e8b5b2f8b6e27ed35e6b7bab7453d1c435d3397cc206cc223</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Asymptotes</topic><topic>Calculus of variations</topic><topic>Control stability</topic><topic>Distribution</topic><topic>Enhanced oil recovery</topic><topic>Flow rates</topic><topic>Flow velocity</topic><topic>Fluid mechanics</topic><topic>Fluids</topic><topic>Gelation</topic><topic>Injection</topic><topic>Instability</topic><topic>Modes</topic><topic>Polymers</topic><topic>Rheological properties</topic><topic>Rheology</topic><topic>Taylor instability</topic><topic>Time dependence</topic><topic>Viscosity</topic><topic>Viscosity ratio</topic><topic>Water pollution</topic><topic>Wavelengths</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Beeson-Jones, Tim H.</creatorcontrib><creatorcontrib>Woods, Andrew W.</creatorcontrib><collection>CrossRef</collection><collection>ProQuest Central (Corporate)</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Water Resources Abstracts</collection><collection>ProQuest Central (purchase pre-March 2016)</collection><collection>Science Database (Alumni Edition)</collection><collection>Technology Research Database</collection><collection>ProQuest SciTech Collection</collection><collection>ProQuest Technology Collection</collection><collection>ProQuest Central (Alumni) (purchase pre-March 2016)</collection><collection>Research Library (Alumni Edition)</collection><collection>Materials Science & Engineering Collection</collection><collection>ProQuest Central (Alumni Edition)</collection><collection>ProQuest One Sustainability</collection><collection>ProQuest Central UK/Ireland</collection><collection>Advanced Technologies & Aerospace Collection</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Technology Collection</collection><collection>Natural Science Collection</collection><collection>Earth, Atmospheric & Aquatic Science Collection</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Engineering Research Database</collection><collection>ProQuest Central Student</collection><collection>Research Library Prep</collection><collection>Aerospace Database</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>SciTech Premium Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>ProQuest Engineering Collection</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Research Library</collection><collection>Science Database</collection><collection>Engineering Database</collection><collection>Research Library (Corporate)</collection><collection>Advanced Technologies & Aerospace Database</collection><collection>ProQuest Advanced Technologies & Aerospace Collection</collection><collection>Earth, Atmospheric & Aquatic Science Database</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>Engineering Collection</collection><collection>ProQuest Central Basic</collection><collection>DELNET Engineering & Technology Collection</collection><jtitle>Journal of fluid mechanics</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Beeson-Jones, Tim H.</au><au>Woods, Andrew W.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Control of viscous instability by variation of injection rate in a fluid with time-dependent rheology</atitle><jtitle>Journal of fluid mechanics</jtitle><addtitle>J. Fluid Mech</addtitle><date>2017-10-25</date><risdate>2017</risdate><volume>829</volume><spage>214</spage><epage>235</epage><pages>214-235</pages><issn>0022-1120</issn><eissn>1469-7645</eissn><abstract>Using variational calculus, we investigate the time-dependent injection rate that minimises the growth of the Saffman–Taylor instability when a finite volume of fluid is injected in a finite time,
$t_{f}$
, into a Hele-Shaw cell. We first consider a planar interface, and show that, with a constant viscosity ratio, the constant injection rate is optimal. When the viscosity of the displacing fluid,
$\unicode[STIX]{x1D707}_{1}(t)$
, gradually increases over time, as may occur with a slowly gelling polymer solution, the optimal injection rate,
$U^{\ast }(t)$
, involves a gradual increase in the flow rate with time. This leads to a smaller initial value of flow rate than the constant injection rate, finishing with a larger value. Such optimisation can lead to a substantial suppression of the instability as compared to the constant injection case if the characteristic gelling time is comparable to
$t_{f}$
. In contrast, for either relatively slow or fast gelling, there is much less benefit in selecting the optimal injection rate,
$U^{\ast }(t)$
, as compared to the constant injection rate. In the case of a constant injection rate from a point source,
$Q$
, then with a constant viscosity ratio the fastest-growing perturbation on the radially spreading front involves axisymmetric modes whose wavenumber increases with time. Approximating the discrete azimuthal modes by a continuous distribution, we find the injection rate that minimises growth,
$Q^{\ast }(t)$
. We find that there is a critical time for injection,
$t_{f}^{\dagger }$
, such that if
$t_{f}>t_{f}^{\dagger }$
then
$Q^{\ast }(t)$
can be chosen so that the interface is always stable. This critical time emerges from the case with an injection rate given by
$Q^{\ast }\sim t^{-1/3}$
. As the total injection time is reduced to values
$t_{f}<t_{f}^{\dagger }$
, the system becomes progressively more unstable, and the optimal injection rate for an idealised continuous distribution of azimuthal modes asymptotes to a flow rate that increases linearly with time. As for the one-dimensional case, if the viscosity of the injection fluid gradually increases over time, then the optimal injection rate has a smaller initial value but gradually increases to larger values than for the analogous constant viscosity problem. If the displacing fluid features shear-thinning rheology, then the optimal injection rate involves a smaller flow rate at early times, although not as large a reduction as in the Newtonian case, and a larger flow rate at late times, although not as large an increase as in the Newtonian case.</abstract><cop>Cambridge, UK</cop><pub>Cambridge University Press</pub><doi>10.1017/jfm.2017.581</doi><tpages>22</tpages><orcidid>https://orcid.org/0000-0002-0253-3260</orcidid><orcidid>https://orcid.org/0000-0002-5098-9940</orcidid></addata></record> |
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subjects | Asymptotes Calculus of variations Control stability Distribution Enhanced oil recovery Flow rates Flow velocity Fluid mechanics Fluids Gelation Injection Instability Modes Polymers Rheological properties Rheology Taylor instability Time dependence Viscosity Viscosity ratio Water pollution Wavelengths |
title | Control of viscous instability by variation of injection rate in a fluid with time-dependent rheology |
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