LrgpV1, PascalFrancis, Checkpoint, bibRecord, 000381

Hydrodynamic regimes of gas-liquid flow in a microreactor channel

Identifieur interne : 000381 ( PascalFrancis/Checkpoint ); précédent : 000380; suivant : 000382

Hydrodynamic regimes of gas-liquid flow in a microreactor channel

Auteurs : R. Pohorecki [Pologne] ; P. Sobieszuk [Pologne] ; K. Kula [Pologne] ; W. Moniuk [Pologne] ; M. Zielinski [Pologne] ; P. Cyganski [Pologne] ; P. Gawinski [Pologne]

Source :

Chemical engineering journal : (1996) [ 1385-8947 ] ; 2008.

RBID : Pascal:08-0055172

Descripteurs français

Pascal (Inist)
- Hydrodynamique, Ecoulement gaz liquide, Ecoulement diphasique, Microréacteur, Angle contact, Tension superficielle, Gaz inerte, Ecoulement liquide, Régime écoulement, Cartographie, Bulle, Aire interfaciale, Transfert masse, Absorption gaz, Réaction chimique.
Wicri :
- topic : Cartographie.

English descriptors

KwdEn :
- Bubble, Cartography, Chemical reaction, Contact angle, Flow regime, Gas absorption, Gas liquid flow, Hydrodynamics, Inert gas, Interfacial area, Liquid flow, Mass transfer, Microreactor, Surface tension, Two phase flow.

Abstract

The hydrodynamic regimes of gas-liquid flow in a microreactor channel have been investigated, using water and ethanol (liquids with different contact angle and surface tension values) and nitrogen as an inert gas. The microreactor was Y-shaped. Experiments were carried out to determine the character of gas and liquid flow ("regime map"). Four main flow types were observed: bubble, slug, slug/annular and annular, the slug regime occupying most of the region investigated. In the second part of the work a criterion for the effectiveness of the gas-liquid interfacial area has been proposed. This criterion determines the mass transfer activity of the interfacial area in the slug regime. Methods of estimation of the parameters necessary to apply the criterion have been outlined.

Affiliations:

Pologne

Links toward previous steps (curation, corpus...)

to stream PascalFrancis, to step Corpus: 000417
to stream PascalFrancis, to step Curation: 000694

Links to Exploration step

Pascal:08-0055172

Le document en format XML

<record><TEI><teiHeader><fileDesc><titleStmt><title xml:lang="en" level="a">Hydrodynamic regimes of gas-liquid flow in a microreactor channel</title>
<author><name sortKey="Pohorecki, R" sort="Pohorecki, R" uniqKey="Pohorecki R" first="R." last="Pohorecki">R. Pohorecki</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Sobieszuk, P" sort="Sobieszuk, P" uniqKey="Sobieszuk P" first="P." last="Sobieszuk">P. Sobieszuk</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Kula, K" sort="Kula, K" uniqKey="Kula K" first="K." last="Kula">K. Kula</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Moniuk, W" sort="Moniuk, W" uniqKey="Moniuk W" first="W." last="Moniuk">W. Moniuk</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Zielinski, M" sort="Zielinski, M" uniqKey="Zielinski M" first="M." last="Zielinski">M. Zielinski</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Cyganski, P" sort="Cyganski, P" uniqKey="Cyganski P" first="P." last="Cyganski">P. Cyganski</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Gawinski, P" sort="Gawinski, P" uniqKey="Gawinski P" first="P." last="Gawinski">P. Gawinski</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
</titleStmt>
<publicationStmt><idno type="wicri:source">INIST</idno>
<idno type="inist">08-0055172</idno>
<date when="2008">2008</date>
<idno type="stanalyst">PASCAL 08-0055172 INIST</idno>
<idno type="RBID">Pascal:08-0055172</idno>
<idno type="wicri:Area/PascalFrancis/Corpus">000417</idno>
<idno type="wicri:Area/PascalFrancis/Curation">000694</idno>
<idno type="wicri:Area/PascalFrancis/Checkpoint">000381</idno>
<idno type="wicri:explorRef" wicri:stream="PascalFrancis" wicri:step="Checkpoint">000381</idno>
</publicationStmt>
<sourceDesc><biblStruct><analytic><title xml:lang="en" level="a">Hydrodynamic regimes of gas-liquid flow in a microreactor channel</title>
<author><name sortKey="Pohorecki, R" sort="Pohorecki, R" uniqKey="Pohorecki R" first="R." last="Pohorecki">R. Pohorecki</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Sobieszuk, P" sort="Sobieszuk, P" uniqKey="Sobieszuk P" first="P." last="Sobieszuk">P. Sobieszuk</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Kula, K" sort="Kula, K" uniqKey="Kula K" first="K." last="Kula">K. Kula</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Moniuk, W" sort="Moniuk, W" uniqKey="Moniuk W" first="W." last="Moniuk">W. Moniuk</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Zielinski, M" sort="Zielinski, M" uniqKey="Zielinski M" first="M." last="Zielinski">M. Zielinski</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Cyganski, P" sort="Cyganski, P" uniqKey="Cyganski P" first="P." last="Cyganski">P. Cyganski</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Gawinski, P" sort="Gawinski, P" uniqKey="Gawinski P" first="P." last="Gawinski">P. Gawinski</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</inist:fA14>
<country>Pologne</country>
<wicri:noRegion>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</wicri:noRegion>
</affiliation>
</author>
</analytic>
<series><title level="j" type="main">Chemical engineering journal : (1996)</title>
<title level="j" type="abbreviated">Chem. eng. j. : (1996)</title>
<idno type="ISSN">1385-8947</idno>
<imprint><date when="2008">2008</date>
</imprint>
</series>
</biblStruct>
</sourceDesc>
<seriesStmt><title level="j" type="main">Chemical engineering journal : (1996)</title>
<title level="j" type="abbreviated">Chem. eng. j. : (1996)</title>
<idno type="ISSN">1385-8947</idno>
</seriesStmt>
</fileDesc>
<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Bubble</term>
<term>Cartography</term>
<term>Chemical reaction</term>
<term>Contact angle</term>
<term>Flow regime</term>
<term>Gas absorption</term>
<term>Gas liquid flow</term>
<term>Hydrodynamics</term>
<term>Inert gas</term>
<term>Interfacial area</term>
<term>Liquid flow</term>
<term>Mass transfer</term>
<term>Microreactor</term>
<term>Surface tension</term>
<term>Two phase flow</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Hydrodynamique</term>
<term>Ecoulement gaz liquide</term>
<term>Ecoulement diphasique</term>
<term>Microréacteur</term>
<term>Angle contact</term>
<term>Tension superficielle</term>
<term>Gaz inerte</term>
<term>Ecoulement liquide</term>
<term>Régime écoulement</term>
<term>Cartographie</term>
<term>Bulle</term>
<term>Aire interfaciale</term>
<term>Transfert masse</term>
<term>Absorption gaz</term>
<term>Réaction chimique</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Cartographie</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front><div type="abstract" xml:lang="en">The hydrodynamic regimes of gas-liquid flow in a microreactor channel have been investigated, using water and ethanol (liquids with different contact angle and surface tension values) and nitrogen as an inert gas. The microreactor was Y-shaped. Experiments were carried out to determine the character of gas and liquid flow ("regime map"). Four main flow types were observed: bubble, slug, slug/annular and annular, the slug regime occupying most of the region investigated. In the second part of the work a criterion for the effectiveness of the gas-liquid interfacial area has been proposed. This criterion determines the mass transfer activity of the interfacial area in the slug regime. Methods of estimation of the parameters necessary to apply the criterion have been outlined.</div>
</front>
</TEI>
<inist><standard h6="B"><pA><fA01 i1="01" i2="1"><s0>1385-8947</s0>
</fA01>
<fA03 i2="1"><s0>Chem. eng. j. : (1996)</s0>
</fA03>
<fA05><s2>135</s2>
</fA05>
<fA06><s3>SUP1</s3>
</fA06>
<fA08 i1="01" i2="1" l="ENG"><s1>Hydrodynamic regimes of gas-liquid flow in a microreactor channel</s1>
</fA08>
<fA09 i1="01" i2="1" l="ENG"><s1>Microreaction Technology, IMRET 9: Proceedings of the Ninth International Conference on Microreaction Technology</s1>
</fA09>
<fA11 i1="01" i2="1"><s1>POHORECKI (R.)</s1>
</fA11>
<fA11 i1="02" i2="1"><s1>SOBIESZUK (P.)</s1>
</fA11>
<fA11 i1="03" i2="1"><s1>KULA (K.)</s1>
</fA11>
<fA11 i1="04" i2="1"><s1>MONIUK (W.)</s1>
</fA11>
<fA11 i1="05" i2="1"><s1>ZIELINSKI (M.)</s1>
</fA11>
<fA11 i1="06" i2="1"><s1>CYGANSKI (P.)</s1>
</fA11>
<fA11 i1="07" i2="1"><s1>GAWINSKI (P.)</s1>
</fA11>
<fA12 i1="01" i2="1"><s1>SCHÜTTE (Rüdiger)</s1>
<s9>ed.</s9>
</fA12>
<fA12 i1="02" i2="1"><s1>RENKEN (Albert)</s1>
<s9>ed.</s9>
</fA12>
<fA12 i1="03" i2="1"><s1>KLEMM (Elias)</s1>
<s9>ed.</s9>
</fA12>
<fA12 i1="04" i2="1"><s1>LIAUW (Marcel A.)</s1>
<s9>ed.</s9>
</fA12>
<fA12 i1="05" i2="1"><s1>MATLOSZ (Michael)</s1>
<s9>ed.</s9>
</fA12>
<fA14 i1="01"><s1>Warsaw University of Technology, Faculty of Chemical and ProcessEngineering</s1>
<s3>POL</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>7 aut.</sZ>
</fA14>
<fA15 i1="01"><s1>Process Technology & Engineering, Evonik Degussa GmbH, Rodenbacher Chaussee 4</s1>
<s2>63457 Hanau (Wolfgang)</s2>
<s3>DEU</s3>
<sZ>1 aut.</sZ>
</fA15>
<fA15 i1="02"><s1>Institute of Chemical Sciences and Engineering, Ecole Polytechnique Fédérale de Lausanne (EPFL), SB-ISIC-LGRC-Station 6, Bâtiment CH / CH J2 500</s1>
<s2>1015 Lausanne</s2>
<s3>CHE</s3>
<sZ>2 aut.</sZ>
</fA15>
<fA15 i1="03"><s1>Chemnitz University of Technology, Faculty of Natural Sciences, Department of Chemical Technology</s1>
<s2>09107 Chemnitz</s2>
<s3>DEU</s3>
<sZ>3 aut.</sZ>
</fA15>
<fA15 i1="04"><s1>Technical Chemistry and Reaction Engineering, ITMC, RWTH Aachen, Worringerweg 1</s1>
<s2>52074 Aachen</s2>
<s3>DEU</s3>
<sZ>4 aut.</sZ>
</fA15>
<fA15 i1="05"><s1>CNRS-ENSIC, Laboratoire des Sciences du Genie Chimique, 1, rue Grandville</s1>
<s2>54001 Nancy</s2>
<s3>FRA</s3>
<sZ>5 aut.</sZ>
</fA15>
<fA20><s2>S185-S190</s2>
</fA20>
<fA21><s1>2008</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>14678</s2>
<s5>354000173568260280</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 2008 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>17 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>08-0055172</s0>
</fA47>
<fA60><s1>P</s1>
<s2>C</s2>
</fA60>
<fA61><s0>A</s0>
</fA61>
<fA64 i1="01" i2="1"><s0>Chemical engineering journal : (1996)</s0>
</fA64>
<fA66 i1="01"><s0>NLD</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>The hydrodynamic regimes of gas-liquid flow in a microreactor channel have been investigated, using water and ethanol (liquids with different contact angle and surface tension values) and nitrogen as an inert gas. The microreactor was Y-shaped. Experiments were carried out to determine the character of gas and liquid flow ("regime map"). Four main flow types were observed: bubble, slug, slug/annular and annular, the slug regime occupying most of the region investigated. In the second part of the work a criterion for the effectiveness of the gas-liquid interfacial area has been proposed. This criterion determines the mass transfer activity of the interfacial area in the slug regime. Methods of estimation of the parameters necessary to apply the criterion have been outlined.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001D07D</s0>
</fC02>
<fC02 i1="02" i2="X"><s0>001D07H</s0>
</fC02>
<fC02 i1="03" i2="X"><s0>001D07G</s0>
</fC02>
<fC02 i1="04" i2="X"><s0>001D07J</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Hydrodynamique</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Hydrodynamics</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Hidrodinámica</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Ecoulement gaz liquide</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Gas liquid flow</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Flujo gas líquido</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Ecoulement diphasique</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Two phase flow</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Flujo difásico</s0>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Microréacteur</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Microreactor</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Microreactor</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Angle contact</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Contact angle</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Angulo contacto</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Tension superficielle</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Surface tension</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Tensión superficial</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Gaz inerte</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Inert gas</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Gas inerte</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Ecoulement liquide</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Liquid flow</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Flujo líquido</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Régime écoulement</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Flow regime</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Régimen flujo</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Cartographie</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Cartography</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Cartografía</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Bulle</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Bubble</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Ampolla</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Aire interfaciale</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Interfacial area</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Superficie interfacial</s0>
<s5>12</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Transfert masse</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Mass transfer</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Transferencia masa</s0>
<s5>13</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Absorption gaz</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Gas absorption</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Absorción gas</s0>
<s5>14</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Réaction chimique</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Chemical reaction</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Reacción química</s0>
<s5>15</s5>
</fC03>
<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>
</inist>
<affiliations><list><country><li>Pologne</li>
</country>
</list>
<tree><country name="Pologne"><noRegion><name sortKey="Pohorecki, R" sort="Pohorecki, R" uniqKey="Pohorecki R" first="R." last="Pohorecki">R. Pohorecki</name>
</noRegion>
<name sortKey="Cyganski, P" sort="Cyganski, P" uniqKey="Cyganski P" first="P." last="Cyganski">P. Cyganski</name>
<name sortKey="Gawinski, P" sort="Gawinski, P" uniqKey="Gawinski P" first="P." last="Gawinski">P. Gawinski</name>
<name sortKey="Kula, K" sort="Kula, K" uniqKey="Kula K" first="K." last="Kula">K. Kula</name>
<name sortKey="Moniuk, W" sort="Moniuk, W" uniqKey="Moniuk W" first="W." last="Moniuk">W. Moniuk</name>
<name sortKey="Sobieszuk, P" sort="Sobieszuk, P" uniqKey="Sobieszuk P" first="P." last="Sobieszuk">P. Sobieszuk</name>
<name sortKey="Zielinski, M" sort="Zielinski, M" uniqKey="Zielinski M" first="M." last="Zielinski">M. Zielinski</name>
</country>
</tree>
</affiliations>
</record>

Pour manipuler ce document sous Unix (Dilib)

EXPLOR_STEP=$WICRI_ROOT/Wicri/Lorraine/explor/LrgpV1/Data/PascalFrancis/Checkpoint

HfdSelect -h $EXPLOR_STEP/biblio.hfd -nk 000381 | SxmlIndent | more

HfdSelect -h $EXPLOR_AREA/Data/PascalFrancis/Checkpoint/biblio.hfd -nk 000381 | SxmlIndent | more

Pour mettre un lien sur cette page dans le réseau Wicri

{{Explor lien
   |wiki=    Wicri/Lorraine
   |area=    LrgpV1
   |flux=    PascalFrancis
   |étape=   Checkpoint
   |type=    RBID
   |clé=     Pascal:08-0055172
   |texte=   Hydrodynamic regimes of gas-liquid flow in a microreactor channel
}}

This area was generated with Dilib version V0.6.32.
Data generation: Sat Nov 11 15:47:48 2017. Site generation: Wed Mar 6 23:31:34 2024

	Serveur d'exploration sur le LRGP
	Attention, ce site est en cours de développement ! Attention, site généré par des moyens informatiques à partir de corpus bruts. Les informations ne sont donc pas validées.

Serveur d'exploration sur le LRGP

Hydrodynamic regimes of gas-liquid flow in a microreactor channel

Hydrodynamic regimes of gas-liquid flow in a microreactor channel

Source :

Descripteurs français

English descriptors

Abstract

Links toward previous steps (curation, corpus...)

Links to Exploration step

Le document en format XML

Pour manipuler ce document sous Unix (Dilib)

Pour mettre un lien sur cette page dans le réseau Wicri