Solubility of poly(ethylene glycol)nonylphenyl ether in supercritical carbon dioxide
Identifieur interne : 001E59 ( Main/Exploration ); précédent : 001E58; suivant : 001E60Solubility of poly(ethylene glycol)nonylphenyl ether in supercritical carbon dioxide
Auteurs : K. Dimitrov [Bulgarie] ; L. Boyadzhiev [Bulgarie] ; R. Tufeu [France] ; F. Cansell [France] ; D. Barth [France]Source :
- The Journal of Supercritical Fluids [ 0896-8446 ] ; 1998.
Descripteurs français
English descriptors
- KwdEn :
- Batch contactor, Constant pressure, Constant temperature, Contactor, Dimitrov, Elsevier science, Exponential function, Fractionation, Glycol, High pressure, Lower molar masses, Mass fraction, Mass transfer, Mass transfer kinetics, Micrometering valve, Molar, Molar mass, Molar mass distribution, Molecular mass, Nonylphenyl ether, Parent polymer, Polymer, Polymer extracts, Polymer fractionation, Polymer fractions, Polymer solubility increases, Pressure increase, Recuperation vessel, Rotation speed, Separation factor, Solubility, Solubility data, Solubility increase, Solubilized polymer, Solvent, Solvent agitation, Solvent bulk, Solvent density, Solventrich phase, Supercritical, Supercritical carbon dioxide, Supercritical extraction, Supercritical fluids, Uids.
- Teeft :
- Batch contactor, Constant pressure, Constant temperature, Contactor, Dimitrov, Elsevier science, Exponential function, Fractionation, Glycol, High pressure, Lower molar masses, Mass fraction, Mass transfer, Mass transfer kinetics, Micrometering valve, Molar, Molar mass, Molar mass distribution, Molecular mass, Nonylphenyl ether, Parent polymer, Polymer, Polymer extracts, Polymer fractionation, Polymer fractions, Polymer solubility increases, Pressure increase, Recuperation vessel, Rotation speed, Separation factor, Solubility, Solubility data, Solubility increase, Solubilized polymer, Solvent, Solvent agitation, Solvent bulk, Solvent density, Solventrich phase, Supercritical, Supercritical carbon dioxide, Supercritical extraction, Supercritical fluids, Uids.
Abstract
Abstract: The solubility of (polyethylene glycol)nonylphenyl ether (PEG-NPE) of weight average molar mass 2500g/mol in supercritical carbon dioxide was studied and the effects of the main parameters, such as pressure, temperature, and solvent density, were evaluated. The individual i-mer partition coefficients were obtained for all polymer compositions. The kinetics of supercritical extraction of PEG-NPE in a stirred batch contactor were studied also. The polymer extraction rate was investigated as a function of the agitator speed. Mass transfer coefficients of the polymer and those of three selected fractions in a solvent-rich phase were evaluated.
Url:
DOI: 10.1016/S0896-8446(98)00093-X
Affiliations:
- Bulgarie, France
- Grand Est, Lorraine (région), Sofia-ville (oblast), Île-de-France
- Nancy, Sofia, Villetaneuse
- Université Paris 13
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- to stream Istex, to step Checkpoint: 000879
- to stream Main, to step Merge: 002260
- to stream Main, to step Curation: 001E59
Le document en format XML
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<front><div type="abstract" xml:lang="en">Abstract: The solubility of (polyethylene glycol)nonylphenyl ether (PEG-NPE) of weight average molar mass 2500g/mol in supercritical carbon dioxide was studied and the effects of the main parameters, such as pressure, temperature, and solvent density, were evaluated. The individual i-mer partition coefficients were obtained for all polymer compositions. The kinetics of supercritical extraction of PEG-NPE in a stirred batch contactor were studied also. The polymer extraction rate was investigated as a function of the agitator speed. Mass transfer coefficients of the polymer and those of three selected fractions in a solvent-rich phase were evaluated.</div>
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