A thermodynamic model is presented to calculate N2 solubility in pure water (273-590 K and 1-600 bar) and aqueous NaCl solutions (273-400 K, 1-600 bar and 0-6 mol kg-1) with or close to experimental accuracy. This model is based on a semi-empirical equation used to calculate gas phase composition of the H2O-N2 system and a specific particle interaction theory for liquid phase. With the parameters evaluated from N2-H2O-NaCl system and using a simple approach, the model is extended to predict the N2 solubility in seawater accurately. Liquid phase density of N2-H2O-NaCl system at phase equilibrium and the homogenization pressure of fluid inclusions containing N2-H2O-NaCl can be calculated from this model. A computer code is developed for this model and can be downloaded from the website: www.geochem-model.org/programs.htm.
Description
ScienceDirect - Fluid Phase Equilibria : A thermodynamic model for calculating nitrogen solubility, gas phase composition and density of the N2–H2O–NaCl system
%0 Journal Article
%1 Mao2006
%A Mao, Shide
%A Duan, Zhenhao
%D 2006
%J Fluid Phase Equilibria
%K 2006 NaCl aqueous brine solubility
%N 2
%P 103--114
%R 10.1016/j.fluid.2006.07.020
%T A thermodynamic model for calculating nitrogen solubility, gas phase composition and density of the N2-H2O-NaCl system
%U http://dx.doi.org/10.1016/j.fluid.2006.07.020
%V 248
%X A thermodynamic model is presented to calculate N2 solubility in pure water (273-590 K and 1-600 bar) and aqueous NaCl solutions (273-400 K, 1-600 bar and 0-6 mol kg-1) with or close to experimental accuracy. This model is based on a semi-empirical equation used to calculate gas phase composition of the H2O-N2 system and a specific particle interaction theory for liquid phase. With the parameters evaluated from N2-H2O-NaCl system and using a simple approach, the model is extended to predict the N2 solubility in seawater accurately. Liquid phase density of N2-H2O-NaCl system at phase equilibrium and the homogenization pressure of fluid inclusions containing N2-H2O-NaCl can be calculated from this model. A computer code is developed for this model and can be downloaded from the website: www.geochem-model.org/programs.htm.
@article{Mao2006,
abstract = {A thermodynamic model is presented to calculate N2 solubility in pure water (273-590 K and 1-600 bar) and aqueous NaCl solutions (273-400 K, 1-600 bar and 0-6 mol kg-1) with or close to experimental accuracy. This model is based on a semi-empirical equation used to calculate gas phase composition of the H2O-N2 system and a specific particle interaction theory for liquid phase. With the parameters evaluated from N2-H2O-NaCl system and using a simple approach, the model is extended to predict the N2 solubility in seawater accurately. Liquid phase density of N2-H2O-NaCl system at phase equilibrium and the homogenization pressure of fluid inclusions containing N2-H2O-NaCl can be calculated from this model. A computer code is developed for this model and can be downloaded from the website: www.geochem-model.org/programs.htm.},
added-at = {2011-01-19T18:06:51.000+0100},
author = {Mao, Shide and Duan, Zhenhao},
biburl = {https://www.bibsonomy.org/bibtex/263aa87a92962ddb55540cc61e9cc85fd/thorade},
description = {ScienceDirect - Fluid Phase Equilibria : A thermodynamic model for calculating nitrogen solubility, gas phase composition and density of the N2–H2O–NaCl system},
doi = {10.1016/j.fluid.2006.07.020},
interhash = {710f998f2e226d2fbb315f08cc86018b},
intrahash = {63aa87a92962ddb55540cc61e9cc85fd},
issn = {0378-3812},
journal = {Fluid Phase Equilibria},
keywords = {2006 NaCl aqueous brine solubility},
number = 2,
pages = {103--114},
timestamp = {2012-11-02T19:47:14.000+0100},
title = {A thermodynamic model for calculating nitrogen solubility, gas phase composition and density of the N2-H2O-NaCl system},
url = {http://dx.doi.org/10.1016/j.fluid.2006.07.020},
volume = 248,
year = 2006
}