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Microfluidic synthesis and assembly of reactive polymer beads to form new structured polymer materials

Identifieur interne : 000432 ( PascalFrancis/Corpus ); précédent : 000431; suivant : 000433

Microfluidic synthesis and assembly of reactive polymer beads to form new structured polymer materials

Auteurs : Michel Bouquey ; Christophe Serra ; Nicolas Benon ; Laurent Prat ; Georges Hadziioannou

Source :

RBID : Pascal:08-0055157

Descripteurs français

English descriptors

Abstract

Monodisperse and size-controlled polymer particles were produced without surfactant or washcoat from O/W monomer emulsions and "on the fly" polymerization under UV irradiation in a very simple needle/tubing system. The effect of the viscosity of the continuous phase on the size of final particles was investigated. The capillary number ratio was found to be relevant to predict the size of the droplets. A relation between dimensionless numbers predicts particle diameter as a function of the needle inner diameter and both velocity and viscosity ratios of continuous and dispersed phases. A functional comonomer was incorporated in the monomer phase so as to obtain polymer microparticles bearing reactive groups on their surface. Polymer beads necklaces were thus formed by linking polymer particles together.

Notice en format standard (ISO 2709)

Pour connaître la documentation sur le format Inist Standard.

pA  
A01 01  1    @0 1385-8947
A03   1    @0 Chem. eng. j. : (1996)
A05       @2 135
A06       @3 SUP1
A08 01  1  ENG  @1 Microfluidic synthesis and assembly of reactive polymer beads to form new structured polymer materials
A09 01  1  ENG  @1 Microreaction Technology, IMRET 9: Proceedings of the Ninth International Conference on Microreaction Technology
A11 01  1    @1 BOUQUEY (Michel)
A11 02  1    @1 SERRA (Christophe)
A11 03  1    @1 BENON (Nicolas)
A11 04  1    @1 PRAT (Laurent)
A11 05  1    @1 HADZIIOANNOU (Georges)
A12 01  1    @1 SCHÜTTE (Rüdiger) @9 ed.
A12 02  1    @1 RENKEN (Albert) @9 ed.
A12 03  1    @1 KLEMM (Elias) @9 ed.
A12 04  1    @1 LIAUW (Marcel A.) @9 ed.
A12 05  1    @1 MATLOSZ (Michael) @9 ed.
A14 01      @1 Laboratoire d'Ingénierie des Polymères pour les Hautes Technologies, CNRS UMR 7165, ECPM, 25 rue Becquerel @2 67087 Strasbourg @3 FRA @Z 1 aut. @Z 2 aut. @Z 3 aut. @Z 5 aut.
A14 02      @1 Laboratoire de Génie Chimique, CNRS UMR 5503, INPT, 5 rue Paulin Talabot @2 31106 Toulouse @3 FRA @Z 4 aut.
A15 01      @1 Process Technology & Engineering, Evonik Degussa GmbH, Rodenbacher Chaussee 4 @2 63457 Hanau (Wolfgang) @3 DEU @Z 1 aut.
A15 02      @1 Institute of Chemical Sciences and Engineering, Ecole Polytechnique Fédérale de Lausanne (EPFL), SB-ISIC-LGRC-Station 6, Bâtiment CH / CH J2 500 @2 1015 Lausanne @3 CHE @Z 2 aut.
A15 03      @1 Chemnitz University of Technology, Faculty of Natural Sciences, Department of Chemical Technology @2 09107 Chemnitz @3 DEU @Z 3 aut.
A15 04      @1 Technical Chemistry and Reaction Engineering, ITMC, RWTH Aachen, Worringerweg 1 @2 52074 Aachen @3 DEU @Z 4 aut.
A15 05      @1 CNRS-ENSIC, Laboratoire des Sciences du Genie Chimique, 1, rue Grandville @2 54001 Nancy @3 FRA @Z 5 aut.
A20       @2 S93-S98
A21       @1 2008
A23 01      @0 ENG
A43 01      @1 INIST @2 14678 @5 354000173568260130
A44       @0 0000 @1 © 2008 INIST-CNRS. All rights reserved.
A45       @0 29 ref.
A47 01  1    @0 08-0055157
A60       @1 P @2 C
A61       @0 A
A64 01  1    @0 Chemical engineering journal : (1996)
A66 01      @0 NLD
C01 01    ENG  @0 Monodisperse and size-controlled polymer particles were produced without surfactant or washcoat from O/W monomer emulsions and "on the fly" polymerization under UV irradiation in a very simple needle/tubing system. The effect of the viscosity of the continuous phase on the size of final particles was investigated. The capillary number ratio was found to be relevant to predict the size of the droplets. A relation between dimensionless numbers predicts particle diameter as a function of the needle inner diameter and both velocity and viscosity ratios of continuous and dispersed phases. A functional comonomer was incorporated in the monomer phase so as to obtain polymer microparticles bearing reactive groups on their surface. Polymer beads necklaces were thus formed by linking polymer particles together.
C02 01  X    @0 001D07H
C03 01  X  FRE  @0 Microfluidique @5 01
C03 01  X  ENG  @0 Microfluidics @5 01
C03 01  X  SPA  @0 Microfluidic @5 01
C03 02  X  FRE  @0 Agent surface @2 FX @5 02
C03 02  X  ENG  @0 Surfactant @2 FX @5 02
C03 02  X  SPA  @0 Agente superficie @2 FX @5 02
C03 03  X  FRE  @0 Emulsion @5 03
C03 03  X  ENG  @0 Emulsion @5 03
C03 03  X  SPA  @0 Emulsión @5 03
C03 04  X  FRE  @0 Polymérisation @5 04
C03 04  X  ENG  @0 Polymerization @5 04
C03 04  X  SPA  @0 Polimerización @5 04
C03 05  X  FRE  @0 Rayonnement UV @5 05
C03 05  X  ENG  @0 Ultraviolet radiation @5 05
C03 05  X  SPA  @0 Radiación ultravioleta @5 05
C03 06  X  FRE  @0 Viscosité @5 06
C03 06  X  ENG  @0 Viscosity @5 06
C03 06  X  SPA  @0 Viscosidad @5 06
C03 07  X  FRE  @0 Phase continue @5 07
C03 07  X  ENG  @0 Continuous phase @5 07
C03 07  X  SPA  @0 Fase continua @5 07
C03 08  X  FRE  @0 Gouttelette @5 08
C03 08  X  ENG  @0 Droplet @5 08
C03 08  X  SPA  @0 Gotita @5 08
C03 09  X  FRE  @0 Phase dispersée @5 09
C03 09  X  ENG  @0 Dispersed phase @5 09
C03 09  X  SPA  @0 Fase dispersada @5 09
C03 10  X  FRE  @0 Microparticule @5 10
C03 10  X  ENG  @0 Microparticle @5 10
C03 10  X  SPA  @0 Micropartícula @5 10
C03 11  X  FRE  @0 Microréacteur @5 11
C03 11  X  ENG  @0 Microreactor @5 11
C03 11  X  SPA  @0 Microreactor @5 11
C07 01  X  FRE  @0 Mécanique fluide
C07 01  X  ENG  @0 Fluid mechanics
C07 01  X  SPA  @0 Mecánica flúido
N21       @1 028
N44 01      @1 OTO
N82       @1 OTO
pR  
A30 01  1  ENG  @1 IMRET 9 : International Conference on Microreaction Technology @2 9 @3 Potsdam DEU @4 2006-09-06

Format Inist (serveur)

NO : PASCAL 08-0055157 INIST
ET : Microfluidic synthesis and assembly of reactive polymer beads to form new structured polymer materials
AU : BOUQUEY (Michel); SERRA (Christophe); BENON (Nicolas); PRAT (Laurent); HADZIIOANNOU (Georges); SCHÜTTE (Rüdiger); RENKEN (Albert); KLEMM (Elias); LIAUW (Marcel A.); MATLOSZ (Michael)
AF : Laboratoire d'Ingénierie des Polymères pour les Hautes Technologies, CNRS UMR 7165, ECPM, 25 rue Becquerel/67087 Strasbourg/France (1 aut., 2 aut., 3 aut., 5 aut.); Laboratoire de Génie Chimique, CNRS UMR 5503, INPT, 5 rue Paulin Talabot/31106 Toulouse/France (4 aut.); Process Technology & Engineering, Evonik Degussa GmbH, Rodenbacher Chaussee 4/63457 Hanau (Wolfgang)/Allemagne (1 aut.); Institute of Chemical Sciences and Engineering, Ecole Polytechnique Fédérale de Lausanne (EPFL), SB-ISIC-LGRC-Station 6, Bâtiment CH / CH J2 500/1015 Lausanne/Suisse (2 aut.); Chemnitz University of Technology, Faculty of Natural Sciences, Department of Chemical Technology/09107 Chemnitz/Allemagne (3 aut.); Technical Chemistry and Reaction Engineering, ITMC, RWTH Aachen, Worringerweg 1/52074 Aachen/Allemagne (4 aut.); CNRS-ENSIC, Laboratoire des Sciences du Genie Chimique, 1, rue Grandville/54001 Nancy/France (5 aut.)
DT : Publication en série; Congrès; Niveau analytique
SO : Chemical engineering journal : (1996); ISSN 1385-8947; Pays-Bas; Da. 2008; Vol. 135; No. SUP1; S93-S98; Bibl. 29 ref.
LA : Anglais
EA : Monodisperse and size-controlled polymer particles were produced without surfactant or washcoat from O/W monomer emulsions and "on the fly" polymerization under UV irradiation in a very simple needle/tubing system. The effect of the viscosity of the continuous phase on the size of final particles was investigated. The capillary number ratio was found to be relevant to predict the size of the droplets. A relation between dimensionless numbers predicts particle diameter as a function of the needle inner diameter and both velocity and viscosity ratios of continuous and dispersed phases. A functional comonomer was incorporated in the monomer phase so as to obtain polymer microparticles bearing reactive groups on their surface. Polymer beads necklaces were thus formed by linking polymer particles together.
CC : 001D07H
FD : Microfluidique; Agent surface; Emulsion; Polymérisation; Rayonnement UV; Viscosité; Phase continue; Gouttelette; Phase dispersée; Microparticule; Microréacteur
FG : Mécanique fluide
ED : Microfluidics; Surfactant; Emulsion; Polymerization; Ultraviolet radiation; Viscosity; Continuous phase; Droplet; Dispersed phase; Microparticle; Microreactor
EG : Fluid mechanics
SD : Microfluidic; Agente superficie; Emulsión; Polimerización; Radiación ultravioleta; Viscosidad; Fase continua; Gotita; Fase dispersada; Micropartícula; Microreactor
LO : INIST-14678.354000173568260130
ID : 08-0055157

Links to Exploration step

Pascal:08-0055157

Le document en format XML

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<fC01 i1="01" l="ENG">
<s0>Monodisperse and size-controlled polymer particles were produced without surfactant or washcoat from O/W monomer emulsions and "on the fly" polymerization under UV irradiation in a very simple needle/tubing system. The effect of the viscosity of the continuous phase on the size of final particles was investigated. The capillary number ratio was found to be relevant to predict the size of the droplets. A relation between dimensionless numbers predicts particle diameter as a function of the needle inner diameter and both velocity and viscosity ratios of continuous and dispersed phases. A functional comonomer was incorporated in the monomer phase so as to obtain polymer microparticles bearing reactive groups on their surface. Polymer beads necklaces were thus formed by linking polymer particles together.</s0>
</fC01>
<fC02 i1="01" i2="X">
<s0>001D07H</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE">
<s0>Microfluidique</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG">
<s0>Microfluidics</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA">
<s0>Microfluidic</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE">
<s0>Agent surface</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG">
<s0>Surfactant</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA">
<s0>Agente superficie</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE">
<s0>Emulsion</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG">
<s0>Emulsion</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA">
<s0>Emulsión</s0>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE">
<s0>Polymérisation</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG">
<s0>Polymerization</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA">
<s0>Polimerización</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE">
<s0>Rayonnement UV</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG">
<s0>Ultraviolet radiation</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA">
<s0>Radiación ultravioleta</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE">
<s0>Viscosité</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG">
<s0>Viscosity</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA">
<s0>Viscosidad</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE">
<s0>Phase continue</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG">
<s0>Continuous phase</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA">
<s0>Fase continua</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE">
<s0>Gouttelette</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG">
<s0>Droplet</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA">
<s0>Gotita</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE">
<s0>Phase dispersée</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG">
<s0>Dispersed phase</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA">
<s0>Fase dispersada</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE">
<s0>Microparticule</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG">
<s0>Microparticle</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA">
<s0>Micropartícula</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE">
<s0>Microréacteur</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG">
<s0>Microreactor</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA">
<s0>Microreactor</s0>
<s5>11</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE">
<s0>Mécanique fluide</s0>
</fC07>
<fC07 i1="01" i2="X" l="ENG">
<s0>Fluid mechanics</s0>
</fC07>
<fC07 i1="01" i2="X" l="SPA">
<s0>Mecánica flúido</s0>
</fC07>
<fN21>
<s1>028</s1>
</fN21>
<fN44 i1="01">
<s1>OTO</s1>
</fN44>
<fN82>
<s1>OTO</s1>
</fN82>
</pA>
<pR>
<fA30 i1="01" i2="1" l="ENG">
<s1>IMRET 9 : International Conference on Microreaction Technology</s1>
<s2>9</s2>
<s3>Potsdam DEU</s3>
<s4>2006-09-06</s4>
</fA30>
</pR>
</standard>
<server>
<NO>PASCAL 08-0055157 INIST</NO>
<ET>Microfluidic synthesis and assembly of reactive polymer beads to form new structured polymer materials</ET>
<AU>BOUQUEY (Michel); SERRA (Christophe); BENON (Nicolas); PRAT (Laurent); HADZIIOANNOU (Georges); SCHÜTTE (Rüdiger); RENKEN (Albert); KLEMM (Elias); LIAUW (Marcel A.); MATLOSZ (Michael)</AU>
<AF>Laboratoire d'Ingénierie des Polymères pour les Hautes Technologies, CNRS UMR 7165, ECPM, 25 rue Becquerel/67087 Strasbourg/France (1 aut., 2 aut., 3 aut., 5 aut.); Laboratoire de Génie Chimique, CNRS UMR 5503, INPT, 5 rue Paulin Talabot/31106 Toulouse/France (4 aut.); Process Technology & Engineering, Evonik Degussa GmbH, Rodenbacher Chaussee 4/63457 Hanau (Wolfgang)/Allemagne (1 aut.); Institute of Chemical Sciences and Engineering, Ecole Polytechnique Fédérale de Lausanne (EPFL), SB-ISIC-LGRC-Station 6, Bâtiment CH / CH J2 500/1015 Lausanne/Suisse (2 aut.); Chemnitz University of Technology, Faculty of Natural Sciences, Department of Chemical Technology/09107 Chemnitz/Allemagne (3 aut.); Technical Chemistry and Reaction Engineering, ITMC, RWTH Aachen, Worringerweg 1/52074 Aachen/Allemagne (4 aut.); CNRS-ENSIC, Laboratoire des Sciences du Genie Chimique, 1, rue Grandville/54001 Nancy/France (5 aut.)</AF>
<DT>Publication en série; Congrès; Niveau analytique</DT>
<SO>Chemical engineering journal : (1996); ISSN 1385-8947; Pays-Bas; Da. 2008; Vol. 135; No. SUP1; S93-S98; Bibl. 29 ref.</SO>
<LA>Anglais</LA>
<EA>Monodisperse and size-controlled polymer particles were produced without surfactant or washcoat from O/W monomer emulsions and "on the fly" polymerization under UV irradiation in a very simple needle/tubing system. The effect of the viscosity of the continuous phase on the size of final particles was investigated. The capillary number ratio was found to be relevant to predict the size of the droplets. A relation between dimensionless numbers predicts particle diameter as a function of the needle inner diameter and both velocity and viscosity ratios of continuous and dispersed phases. A functional comonomer was incorporated in the monomer phase so as to obtain polymer microparticles bearing reactive groups on their surface. Polymer beads necklaces were thus formed by linking polymer particles together.</EA>
<CC>001D07H</CC>
<FD>Microfluidique; Agent surface; Emulsion; Polymérisation; Rayonnement UV; Viscosité; Phase continue; Gouttelette; Phase dispersée; Microparticule; Microréacteur</FD>
<FG>Mécanique fluide</FG>
<ED>Microfluidics; Surfactant; Emulsion; Polymerization; Ultraviolet radiation; Viscosity; Continuous phase; Droplet; Dispersed phase; Microparticle; Microreactor</ED>
<EG>Fluid mechanics</EG>
<SD>Microfluidic; Agente superficie; Emulsión; Polimerización; Radiación ultravioleta; Viscosidad; Fase continua; Gotita; Fase dispersada; Micropartícula; Microreactor</SD>
<LO>INIST-14678.354000173568260130</LO>
<ID>08-0055157</ID>
</server>
</inist>
</record>

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