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The Sixth Industrial Fluid Properties Simulation ChallengeSubmitted by site admin on Wed, 2010-06-16 16:21.
Objective The objective of this challenge is to test the ability of computer modeling to predict the mutual solubility in liquid-liquid equilibria of water and a glycol ether as a function of temperature. Timeline
June 16, 2010: problem announced
Background Unlike most organic solvents, glycol ethers and glycol diethers exhibit an “inverse solubility” relationship with water. That is, in the range of normal process conditions they become more compatible as they are cooled and are completely miscible below the lower critical solution temperature (LCST). This behavior is typically rationalized in terms of a temperature-dependent balance between hydrophobic and hydrophilic interactions. This balance of interactions in aqueous solutions is of great scientific and practical importance as a key driving force in phenomena like self-assembly and protein folding. Glycol ethers are used in a wide range of product formulations and industrial processes. For example, they are used as solvents and co-solvents in both organic- and water-based formulations for applications such as cleaning solutions, paints, coatings, and inks. A variety of other novel applications have been proposed that take advantage of the inverse solubility behavior. Dipropylene glycol dimethyl ether (DPGDME) is unique among common propylene-oxide-based solvents in that it has no hydroxyl functionality. This means it is relatively inert and can be used in systems that are proton-sensitive (e.g., water-based polyurethane coatings). Although mutual solubility data for liquid−liquid equilibrium (LLE) for a number of water + ethylene glycol ether and water + propylene glycol ether mixtures have been reported in the literature [1], the temperature-dependence of water + dipropylene glycol dimethyl ether mutual solubility has not been reported. Data are available at 298 K for the commercial product PROGLYDE DMM TM where the solubility of DPGDME in water is reported to be 35 wt % and of water in DPGDME to be 4.5 wt % [2]. Proglyde DMM (C8H18O3) consists of 3 structural isomers, two of which are the major components that occur in approximately equal amounts):
A typical composition of PROGYLDE DMM is 50 % I, 47 % II, and 3 % III. CAS # 111109-77-4 can represent any of the three isomers or mixtures thereof. Studies of phase equilibria by molecular simulation have become relatively common, employing techniques such as Gibbs Ensemble Monte Carlo [3] and Grand Canonical Monte Carlo with histogram reweighting [4]. Typically, these methods have been employed to study vapor-liquid equilibria in particular and to develop general, transferable force fields (potential energy models) that are reasonably accurate over a wide range of state conditions. Only rarely have these methods been used to predict liquid-liquid equilibria of realistic, moderately complex molecular systems. More commonly, molecular dynamics simulations have been used to study liquid-liquid systems, but those studies have typically focused on the details of structure and interactions at the interface and not on predicting the bulk phase compositions of the coexisting phases. Therefore, assessing the capability of molecular simulation methods and force fields to accurately predict liquid-liquid phase equilibria for practically relevant and moderately complex chemical systems is of interest in establishing more clearly the state-of-the-art capability in this application area. Challenge For the PROGLYDE DMM + water system, compute the mutual solubilities in liquid-liquid equilibria at temperatures of 283, 323, 333 and 353 K and atmospheric pressure. Rules of the Game
Challenge Scoring Entries will be scored by comparing the predicted composition of each phase (wt % PROGLYDE DMM) to measured data. Full credit will be awarded for a prediction that falls within the experimental uncertainty. A linear interpolation of partial credit will be awarded for predictions with an absolute deviation above the minimum threshold and a maximum of X % (to be determined). No points will be awarded for prediction above the maximum deviation. Each of the four state points will be weighted equally (i.e. represent 25 % of the total points available). Other Entry Guidelines
References [1] S.P. Christensen, F.A. Donate, T.C. Frank, R.J. LaTulip, L.C. Wilson, Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems , J. Chem. Eng. Data, 50 (2005) 869-877. [2] Proglyde DMM Product Information [3] A.Z. Panagiotopoulos, Direct determination of phase coexistence properties of fluids by Monte Carlo simulation in a new ensemble , Mol. Phys., 61 (1987) 813-826. [4] A.M. Ferrenberg, R.H. Swendsen, New Monte Carlo technique for studying phase transitions , Phys. Rev. Lett., 61 (1988) 2635-2638. |