1990
DOI: 10.1021/je00059a018
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Neighbor effects on the group contribution method: infinite dilution activity coefficients of binary systems containing primary amines and alcohols

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Cited by 27 publications
(13 citation statements)
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“…Modeling of water absorption by atmospheric organic aerosol is extremely difficult due to the complexity of the organic chemical composition confounded by the lack of thermodynamic data and models applicable to organic compounds of various structures and their mixtures. Several attempts have been made to use semiempirical models to predict water absorption by organics using information on the functional organic groups [ Ansari and Pandis , 2000; Clegg et al , 2001; Griffin et al , 2003; Ming and Russell , 2002; Pividal and Sandler , 1990]. Unfortunately, no information on functional groups of organic compounds in ambient aerosol is available in our study.…”
Section: Resultsmentioning
confidence: 99%
“…Modeling of water absorption by atmospheric organic aerosol is extremely difficult due to the complexity of the organic chemical composition confounded by the lack of thermodynamic data and models applicable to organic compounds of various structures and their mixtures. Several attempts have been made to use semiempirical models to predict water absorption by organics using information on the functional organic groups [ Ansari and Pandis , 2000; Clegg et al , 2001; Griffin et al , 2003; Ming and Russell , 2002; Pividal and Sandler , 1990]. Unfortunately, no information on functional groups of organic compounds in ambient aerosol is available in our study.…”
Section: Resultsmentioning
confidence: 99%
“…The measurement data available in the literature for systems with alcohols and amines with cycloaliphatic structures are listed in Table . For the system CHA + methanol, enthalpies of mixing at 298.15 K for the whole concentration range are available from Mato and Berrueta and VLE data at atmospheric pressure from Kato et al The only data set with activity coefficients at infinite dilution was published for the system CHA + pentanol by Pividal and Sandler . Isobaric VLE data for the systems CHA with the primary alcohols ethanol, propanol, or butanol were published by a Kato et al and Zlacky et al Isobaric VLE data for the system CHA + 2-propanol were published by Kato et al For the system CHA + cyclohexanol (CHOH), isobaric VLE data were published by Zharikov et al and Novak et al and isothermal VLE data by Mörke et al…”
Section: Methodsmentioning
confidence: 99%
“…20 and VLE data at atmospheric pressure from Kato et al 21 The only data set with activity coefficients at infinite dilution was published for the system CHA + pentanol by Pividal and Sandler. 22 Isobaric VLE data for the systems CHA with the primary alcohols ethanol, propanol, or butanol were published by a Kato et al 21 and Zlacky et al 23 Isobaric VLE data for the system CHA + 2-propanol were published by Kato et al 21 For the system CHA + cyclohexanol (CHOH), isobaric VLE data were published by Zharikov et al 24 and Novak et al 25 and isothermal VLE data by Morke et al 26 It becomes obvious that data are almost exclusively available with short-chain linear alcohols or with CHOH. Other cycloaliphatic amines than CHA were not used.…”
Section: Introductionmentioning
confidence: 99%
“…At low pressures, the fugacity of component i in a binary liquid mixture can be expressed by the relationships ft = ypfl (i) = Hij/Pt which, for a binary mixture, gives (6) = H1i2/P! (7) 72 -H2ii/P| (8) According to Pierotti (1976) and to Geller et al (1976) where 17 is the molar volume of the solvent.…”
Section: Thermodynamic Frameworkmentioning
confidence: 99%
“…0 Units: a, cm3 x 1024; t/k, K; , Á; µ, D. AAPD, average absolute percent deviation on second virial coefficient data. 6 All components with µ < 1 were considered nonpolar and µ was set to 0.…”
Section: Thermodynamic Frameworkmentioning
confidence: 99%