The third industrial fluid properties simulation challenge

被引:29
作者
Case, Fiona H.
Brennan, John
Chaka, Anne
Dobbs, Kerwin D.
Friend, Daniel G.
Frurip, David
Gordon, Peter A.
Moore, Jonathan
Mountain, Raymond D. [1 ]
Olson, James
Ross, Richard B.
Schiller, Martin
Shen, Vincent K.
机构
[1] Case Sci, Essex Jct, VT USA
[2] Army Res Lab, Aberdeen Proving Ground, MD USA
[3] NIST, Gaithersburg, MD 20899 USA
[4] DuPont Co Inc, Wilmington, DE USA
[5] NIST, Boulder, CO USA
[6] Dow Chem Co USA, Midland, MI USA
[7] ExxonMobil Co, Annandale, NJ USA
[8] Dow Chem Co USA, Charleston, WV USA
[9] 3M Co, St Paul, MN USA
关键词
molecular simulation; VLE; phase equilibria; viscosity; statistical mechanics; molecular dynamics; Monte Carlo; VAPOR-LIQUID-EQUILIBRIA; MOLECULAR-DYNAMICS SIMULATION; HENRYS LAW CONSTANTS; PHASE-EQUILIBRIA; FORCE-FIELD; SHEAR VISCOSITY; COSMO-RS; TRANSFERABLE POTENTIALS; PREDICTION; MIXTURES;
D O I
10.1016/j.fluid.2007.08.021
中图分类号
O414.1 [热力学];
学科分类号
摘要
The third industrial fluid properties simulation challenge was held from March to September 2006. As in the previous two events contestants were challenged to predict specific, indutrially relevant, properties of fluid systems. Their efforts were judged based on the agreement of the predicted values with previously unpublished experimental data (provided by researchers at ExxonMobil and DuPont). The focus of this contest was on the transferability of modeling methods-the ability to predict properties for materials that are chemically different, or at different state points, to those used in model parameterization and validation. Nine groups attempted to compute bubble point pressures for mixtures of 1, 1, 1,2,3,3,3heptafluoropropane (HFC-227ea) and ethanol at 343 K, given data for mixtures at 283 K, and given the pure component vapor pressures. They used a range of different techniques including statistical mechanical and molecular simulations-based approaches. Four of the groups were recognized for providing predictions that were significantly more accurate than would be obtained by extrapolation using the NRTL model (the standard engineering approach). Three groups undertook the more challenging "molecular transferability" problem, attempting to predict shear viscosities at two different state points for a range of diols and triols for which little experimental data was available. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:153 / 163
页数:11
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