Characterization of highly boiling hydrocarbons with very low pressure data
Identifieur interne :
001027 ( PascalFrancis/Corpus );
précédent :
001026;
suivant :
001028
Characterization of highly boiling hydrocarbons with very low pressure data
Auteurs : M. Rogalski ;
L. Schuffenecker ;
E. Neau ;
J.-N. Jaubert ;
J. JoseSource :
-
Fluid phase equilibria [ 0378-3812 ] ; 1993.
RBID : Pascal:93-0578003
Descripteurs français
English descriptors
Abstract
The method we recently described for estimating critical properties of hydrocarbons using experimental vapour pressure and density data (VPD method) was modified in order to be applicable to compounds with very low vapour pressures. Accordingly, it was possible to estimate the normal boiling temperature, critical temperature and critical pressure of every hydrocarbon for which vapour pressures and liquid densities were known. In the case of high molecular weight compounds, the critical parameters of which are beyond the scope of reliable experiments, this method constitutes a valuable source of information
Notice en format standard (ISO 2709)
Pour connaître la documentation sur le format Inist Standard.
| pA |
| A01 | 01 | 1 | | @0 0378-3812 |
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| A02 | 01 | | | @0 FPEQDT |
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| A03 | | 1 | | @0 Fluid phase equilib. |
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| A05 | | | | @2 87 |
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| A06 | | | | @2 1 |
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| A08 | 01 | 1 | ENG | @1 Characterization of highly boiling hydrocarbons with very low pressure data |
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| A11 | 01 | 1 | | @1 ROGALSKI (M.) |
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| A11 | 02 | 1 | | @1 SCHUFFENECKER (L.) |
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| A11 | 03 | 1 | | @1 NEAU (E.) |
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| A11 | 04 | 1 | | @1 JAUBERT (J.-N.) |
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| A11 | 05 | 1 | | @1 JOSE (J.) |
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| A12 | 01 | 1 | | @1 RENON (H.) @9 ed. |
|---|
| A14 | 01 | | | @1 INPL-ENSIC, lab. thermodynamique chimique appliquée @2 54001 Nancy @3 FRA @Z 1 aut. @Z 2 aut. |
|---|
| A14 | 02 | | | @1 Fac. sci. Luminy, lab. chimie physique @2 13288 Marseille @3 FRA @Z 3 aut. @Z 4 aut. |
|---|
| A14 | 03 | | | @1 Univ. Claude Bernard, lab. chimie analytique @2 69622 Villeurbanne @3 FRA @Z 5 aut. |
|---|
| A15 | 01 | | | @1 Ecole mines @2 75006 Paris @3 FRA |
|---|
| A18 | 01 | 1 | | @1 Italian Association of Physical-Chemistry @3 ITA @9 patr. |
|---|
| A18 | 02 | 1 | | @1 Italian Association of Calorimetry and Thermal Analysis @3 ITA @9 patr. |
|---|
| A18 | 03 | 1 | | @1 Interdivisional Group of Calorimetry and Thermal Analysis @3 INC @9 patr. |
|---|
| A20 | | | | @1 89-98 |
|---|
| A21 | | | | @1 1993 |
|---|
| A23 | 01 | | | @0 ENG |
|---|
| A43 | 01 | | | @1 INIST @2 17569 @5 354000034864960050 |
|---|
| A44 | | | | @0 0000 |
|---|
| A45 | | | | @0 17 ref. |
|---|
| A47 | 01 | 1 | | @0 93-0578003 |
|---|
| A60 | | | | @1 P @2 C |
|---|
| A61 | | | | @0 A |
|---|
| A64 | | 1 | | @0 Fluid phase equilibria |
|---|
| A66 | 01 | | | @0 NLD |
|---|
| C01 | 01 | | ENG | @0 The method we recently described for estimating critical properties of hydrocarbons using experimental vapour pressure and density data (VPD method) was modified in order to be applicable to compounds with very low vapour pressures. Accordingly, it was possible to estimate the normal boiling temperature, critical temperature and critical pressure of every hydrocarbon for which vapour pressures and liquid densities were known. In the case of high molecular weight compounds, the critical parameters of which are beyond the scope of reliable experiments, this method constitutes a valuable source of information |
|---|
| C02 | 01 | X | | @0 001B10D04 |
|---|
| C03 | 01 | X | FRE | @0 Propriété critique @5 02 |
|---|
| C03 | 01 | X | ENG | @0 Critical property @5 02 |
|---|
| C03 | 01 | X | SPA | @0 Propiedad crítica @5 02 |
|---|
| C03 | 02 | X | FRE | @0 Point ébullition @5 03 |
|---|
| C03 | 02 | X | ENG | @0 Boiling point @5 03 |
|---|
| C03 | 02 | X | GER | @0 Siedetemperatur @5 03 |
|---|
| C03 | 02 | X | SPA | @0 Punto ebullición @5 03 |
|---|
| C03 | 03 | X | FRE | @0 Température critique @5 04 |
|---|
| C03 | 03 | X | ENG | @0 Critical temperature @5 04 |
|---|
| C03 | 03 | X | SPA | @0 Temperatura crítica @5 04 |
|---|
| C03 | 04 | X | FRE | @0 Pression critique @5 05 |
|---|
| C03 | 04 | X | ENG | @0 Critical pressure @5 05 |
|---|
| C03 | 04 | X | SPA | @0 Presión crítica @5 05 |
|---|
| C03 | 05 | X | FRE | @0 Hydrocarbure @2 NK @2 FX @5 16 |
|---|
| C03 | 05 | X | ENG | @0 Hydrocarbon @2 NK @2 FX @5 16 |
|---|
| C03 | 05 | X | GER | @0 Kohlenwasserstoff @2 NK @2 FX @5 16 |
|---|
| C03 | 05 | X | SPA | @0 Hidrocarburo @2 NK @2 FX @5 16 |
|---|
| N21 | | | | @1 272 |
|---|
|
|---|
| pR |
| A30 | 01 | 1 | ENG | @1 International workshop on thermodynamics of organic mixtures @3 Cagliari ITA @4 1991-06-14 |
|---|
|
|---|
Format Inist (serveur)
| NO : | PASCAL 93-0578003 INIST |
|---|
| ET : | Characterization of highly boiling hydrocarbons with very low pressure data |
|---|
| AU : | ROGALSKI (M.); SCHUFFENECKER (L.); NEAU (E.); JAUBERT (J.-N.); JOSE (J.); RENON (H.) |
|---|
| AF : | INPL-ENSIC, lab. thermodynamique chimique appliquée/54001 Nancy/France (1 aut., 2 aut.); Fac. sci. Luminy, lab. chimie physique/13288 Marseille/France (3 aut., 4 aut.); Univ. Claude Bernard, lab. chimie analytique/69622 Villeurbanne/France (5 aut.); Ecole mines/75006 Paris/France |
|---|
| DT : | Publication en série; Congrès; Niveau analytique |
|---|
| SO : | Fluid phase equilibria; ISSN 0378-3812; Coden FPEQDT; Pays-Bas; Da. 1993; Vol. 87; No. 1; Pp. 89-98; Bibl. 17 ref. |
|---|
| LA : | Anglais |
|---|
| EA : | The method we recently described for estimating critical properties of hydrocarbons using experimental vapour pressure and density data (VPD method) was modified in order to be applicable to compounds with very low vapour pressures. Accordingly, it was possible to estimate the normal boiling temperature, critical temperature and critical pressure of every hydrocarbon for which vapour pressures and liquid densities were known. In the case of high molecular weight compounds, the critical parameters of which are beyond the scope of reliable experiments, this method constitutes a valuable source of information |
|---|
| CC : | 001B10D04 |
|---|
| FD : | Propriété critique; Point ébullition; Température critique; Pression critique; Hydrocarbure |
|---|
| ED : | Critical property; Boiling point; Critical temperature; Critical pressure; Hydrocarbon |
|---|
| GD : | Siedetemperatur; Kohlenwasserstoff |
|---|
| SD : | Propiedad crítica; Punto ebullición; Temperatura crítica; Presión crítica; Hidrocarburo |
|---|
| LO : | INIST-17569.354000034864960050 |
|---|
| ID : | 93-0578003 |
|---|
Links to Exploration step
Pascal:93-0578003
Le document en format XML
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</inist:fA14><series><title level="j" type="main">Fluid phase equilibria</title>
<title level="j" type="abbreviated">Fluid phase equilib.</title>
<idno type="ISSN">0378-3812</idno>
<imprint><date when="1993">1993</date>
</imprint><seriesStmt><title level="j" type="main">Fluid phase equilibria</title>
<title level="j" type="abbreviated">Fluid phase equilib.</title>
<idno type="ISSN">0378-3812</idno>
</seriesStmt><profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Boiling point</term>
<term>Critical pressure</term>
<term>Critical property</term>
<term>Critical temperature</term>
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<term>Point ébullition</term>
<term>Température critique</term>
<term>Pression critique</term>
<term>Hydrocarbure</term>
</keywords><front><div type="abstract" xml:lang="en">The method we recently described for estimating critical properties of hydrocarbons using experimental vapour pressure and density data (VPD method) was modified in order to be applicable to compounds with very low vapour pressures. Accordingly, it was possible to estimate the normal boiling temperature, critical temperature and critical pressure of every hydrocarbon for which vapour pressures and liquid densities were known. In the case of high molecular weight compounds, the critical parameters of which are beyond the scope of reliable experiments, this method constitutes a valuable source of information</div>
</front><inist><standard h6="B"><pA><fA01 i1="01" i2="1"><s0>0378-3812</s0>
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</fA08><fA11 i1="01" i2="1"><s1>ROGALSKI (M.)</s1>
</fA11><fA11 i1="02" i2="1"><s1>SCHUFFENECKER (L.)</s1>
</fA11><fA11 i1="03" i2="1"><s1>NEAU (E.)</s1>
</fA11><fA11 i1="04" i2="1"><s1>JAUBERT (J.-N.)</s1>
</fA11><fA11 i1="05" i2="1"><s1>JOSE (J.)</s1>
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<s9>ed.</s9>
</fA12><fA14 i1="01"><s1>INPL-ENSIC, lab. thermodynamique chimique appliquée</s1>
<s2>54001 Nancy</s2>
<s3>FRA</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</fA14><fA14 i1="02"><s1>Fac. sci. Luminy, lab. chimie physique</s1>
<s2>13288 Marseille</s2>
<s3>FRA</s3>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
</fA14><fA14 i1="03"><s1>Univ. Claude Bernard, lab. chimie analytique</s1>
<s2>69622 Villeurbanne</s2>
<s3>FRA</s3>
<sZ>5 aut.</sZ>
</fA14><fA15 i1="01"><s1>Ecole mines</s1>
<s2>75006 Paris</s2>
<s3>FRA</s3>
</fA15><fA18 i1="01" i2="1"><s1>Italian Association of Physical-Chemistry</s1>
<s3>ITA</s3>
<s9>patr.</s9>
</fA18><fA18 i1="02" i2="1"><s1>Italian Association of Calorimetry and Thermal Analysis</s1>
<s3>ITA</s3>
<s9>patr.</s9>
</fA18><fA18 i1="03" i2="1"><s1>Interdivisional Group of Calorimetry and Thermal Analysis</s1>
<s3>INC</s3>
<s9>patr.</s9>
</fA18><fA20><s1>89-98</s1>
</fA20><fA21><s1>1993</s1>
</fA21><fA23 i1="01"><s0>ENG</s0>
</fA23><fA43 i1="01"><s1>INIST</s1>
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</fA44><fA45><s0>17 ref.</s0>
</fA45><fA47 i1="01" i2="1"><s0>93-0578003</s0>
</fA47><fA60><s1>P</s1>
<s2>C</s2>
</fA60><fA64 i2="1"><s0>Fluid phase equilibria</s0>
</fA64><fA66 i1="01"><s0>NLD</s0>
</fA66><fC01 i1="01" l="ENG"><s0>The method we recently described for estimating critical properties of hydrocarbons using experimental vapour pressure and density data (VPD method) was modified in order to be applicable to compounds with very low vapour pressures. Accordingly, it was possible to estimate the normal boiling temperature, critical temperature and critical pressure of every hydrocarbon for which vapour pressures and liquid densities were known. In the case of high molecular weight compounds, the critical parameters of which are beyond the scope of reliable experiments, this method constitutes a valuable source of information</s0>
</fC01><fC02 i1="01" i2="X"><s0>001B10D04</s0>
</fC02><fC03 i1="01" i2="X" l="FRE"><s0>Propriété critique</s0>
<s5>02</s5>
</fC03><fC03 i1="01" i2="X" l="ENG"><s0>Critical property</s0>
<s5>02</s5>
</fC03><fC03 i1="01" i2="X" l="SPA"><s0>Propiedad crítica</s0>
<s5>02</s5>
</fC03><fC03 i1="02" i2="X" l="FRE"><s0>Point ébullition</s0>
<s5>03</s5>
</fC03><fC03 i1="02" i2="X" l="ENG"><s0>Boiling point</s0>
<s5>03</s5>
</fC03><fC03 i1="02" i2="X" l="GER"><s0>Siedetemperatur</s0>
<s5>03</s5>
</fC03><fC03 i1="02" i2="X" l="SPA"><s0>Punto ebullición</s0>
<s5>03</s5>
</fC03><fC03 i1="03" i2="X" l="FRE"><s0>Température critique</s0>
<s5>04</s5>
</fC03><fC03 i1="03" i2="X" l="ENG"><s0>Critical temperature</s0>
<s5>04</s5>
</fC03><fC03 i1="03" i2="X" l="SPA"><s0>Temperatura crítica</s0>
<s5>04</s5>
</fC03><fC03 i1="04" i2="X" l="FRE"><s0>Pression critique</s0>
<s5>05</s5>
</fC03><fC03 i1="04" i2="X" l="ENG"><s0>Critical pressure</s0>
<s5>05</s5>
</fC03><fC03 i1="04" i2="X" l="SPA"><s0>Presión crítica</s0>
<s5>05</s5>
</fC03><fC03 i1="05" i2="X" l="FRE"><s0>Hydrocarbure</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>16</s5>
</fC03><fC03 i1="05" i2="X" l="ENG"><s0>Hydrocarbon</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>16</s5>
</fC03><fC03 i1="05" i2="X" l="GER"><s0>Kohlenwasserstoff</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>16</s5>
</fC03><fC03 i1="05" i2="X" l="SPA"><s0>Hidrocarburo</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>16</s5>
</fC03><fN21><s1>272</s1>
</fN21><pR><fA30 i1="01" i2="1" l="ENG"><s1>International workshop on thermodynamics of organic mixtures</s1>
<s3>Cagliari ITA</s3>
<s4>1991-06-14</s4>
</fA30><server><NO>PASCAL 93-0578003 INIST</NO>
<ET>Characterization of highly boiling hydrocarbons with very low pressure data</ET>
<AU>ROGALSKI (M.); SCHUFFENECKER (L.); NEAU (E.); JAUBERT (J.-N.); JOSE (J.); RENON (H.)</AU>
<AF>INPL-ENSIC, lab. thermodynamique chimique appliquée/54001 Nancy/France (1 aut., 2 aut.); Fac. sci. Luminy, lab. chimie physique/13288 Marseille/France (3 aut., 4 aut.); Univ. Claude Bernard, lab. chimie analytique/69622 Villeurbanne/France (5 aut.); Ecole mines/75006 Paris/France</AF>
<DT>Publication en série; Congrès; Niveau analytique</DT>
<SO>Fluid phase equilibria; ISSN 0378-3812; Coden FPEQDT; Pays-Bas; Da. 1993; Vol. 87; No. 1; Pp. 89-98; Bibl. 17 ref.</SO>
<LA>Anglais</LA>
<EA>The method we recently described for estimating critical properties of hydrocarbons using experimental vapour pressure and density data (VPD method) was modified in order to be applicable to compounds with very low vapour pressures. Accordingly, it was possible to estimate the normal boiling temperature, critical temperature and critical pressure of every hydrocarbon for which vapour pressures and liquid densities were known. In the case of high molecular weight compounds, the critical parameters of which are beyond the scope of reliable experiments, this method constitutes a valuable source of information</EA>
<CC>001B10D04</CC>
<FD>Propriété critique; Point ébullition; Température critique; Pression critique; Hydrocarbure</FD>
<ED>Critical property; Boiling point; Critical temperature; Critical pressure; Hydrocarbon</ED>
<GD>Siedetemperatur; Kohlenwasserstoff</GD>
<SD>Propiedad crítica; Punto ebullición; Temperatura crítica; Presión crítica; Hidrocarburo</SD>
<LO>INIST-17569.354000034864960050</LO>
<ID>93-0578003</ID>
</server>
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