Add to ORKGAn extended UNIFAC group contribution model for the prediction of activity coefficients in associating mixtures was presented recently (Mengarelli et al.,1999). In the present work the model is applied to solutions containing alcohols, water, carboxylic acids and inert components. The residual UNIFAC local composition term is re-parameterized in order to take into account only dispersive forces between associating and inert functional groups. Good representation of vapor-liquid and liquid-liquid equilibrium, as well as infinite dilution activity coefficients is achieved by using a single set of group interaction parameters
UNIFAC group parameters for the interaction between CH2 and CF2 (c) and CH2 and CF3 were obtained us...
WOS: A1996VU72400006Infinite dilution activity coefficients have been calculated for 24 systems incl...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...
A modified UNIFAC group contribution model for the prediction of activity coefficients in associatin...
http://apps.isiknowledge.com/full_record.do?product=UA&search_mode=GeneralSearch&qid=4&SID=V21Di6Paj...
A modifed UNIFAC group contribution model for the prediction of activity coefficients in associating...
A group contribution model is presented for the prediction of activity coefficients in associating ...
The design of extraction, fractionation and purification processes of natural products requires the ...
In this work, a modified UNIFAC model [1] that explicitly takes into account association effects is ...
In the present work, the group contribution with association equation of state (GCA-EoS) is extended...
http://apps.isiknowledge.com/full_record.do?product=UA&search_mode=GeneralSearch&qid=6&SID=V21Di6Paj...
Group contribution models such as ASOG or UNIFAC were known to be inaccurate in the prediction of in...
The UNIQUAC model for the excess Gibbs energy is modified using chemical theory to account for chain...
Infinite dilution activity coefficients have been calculated for 24 systems including highly non-ide...
At present, at least for engineering purposes, the most successful predictive models for activity co...
UNIFAC group parameters for the interaction between CH2 and CF2 (c) and CH2 and CF3 were obtained us...
WOS: A1996VU72400006Infinite dilution activity coefficients have been calculated for 24 systems incl...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...
A modified UNIFAC group contribution model for the prediction of activity coefficients in associatin...
http://apps.isiknowledge.com/full_record.do?product=UA&search_mode=GeneralSearch&qid=4&SID=V21Di6Paj...
A modifed UNIFAC group contribution model for the prediction of activity coefficients in associating...
A group contribution model is presented for the prediction of activity coefficients in associating ...
The design of extraction, fractionation and purification processes of natural products requires the ...
In this work, a modified UNIFAC model [1] that explicitly takes into account association effects is ...
In the present work, the group contribution with association equation of state (GCA-EoS) is extended...
http://apps.isiknowledge.com/full_record.do?product=UA&search_mode=GeneralSearch&qid=6&SID=V21Di6Paj...
Group contribution models such as ASOG or UNIFAC were known to be inaccurate in the prediction of in...
The UNIQUAC model for the excess Gibbs energy is modified using chemical theory to account for chain...
Infinite dilution activity coefficients have been calculated for 24 systems including highly non-ide...
At present, at least for engineering purposes, the most successful predictive models for activity co...
UNIFAC group parameters for the interaction between CH2 and CF2 (c) and CH2 and CF3 were obtained us...
WOS: A1996VU72400006Infinite dilution activity coefficients have been calculated for 24 systems incl...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...