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Proposal for the 5th Simulation ChallengeSubmitted by site admin on Fri, 2008-02-01 16:25.
This is a proposal for the 5th Industrial Fluid Properties Simulation Challenge problem. Please send you feedback and sugestions to ifpsc@fluidproperties.org by February 15, 2008. Prediction of 1-Octanol-Water Partition and Infinite-Dilution Activity Coefficients Objective: The objective of this Challenge of the IFPSC is to test the ability of computer modeling (any method) to predict 1-Octanol-Water Partition (ko/w) and Infinite-Dilution Activity Coefficients (gam-inf). Background: The ability of computer modeling to predict properties that are challenging, inaccessible to experiment, or simply missing is often used as a justification for its development. We want to test/promote/validate this capability. Thermophysical properties, phase equilibria, and solution chemistries are the underlying physical and chemical phenomena of industrial chemical processes. Rigorous thermodynamic modeling of such phenomena establishes a sound and scientific foundation for simulation of chemical processes and subsequent process development, optimization and control. There are three main aspects of applied thermodynamics and phase equilibria of interest:
In the first 4 challenges we have tested these aspects with varying results. For example, one task was to predict pure component vapor pressures. Another was to predict vapor-liquid equilibria (VLE) of binary mixtures at varying conditions. In this 5th challenge we want to refocus on aspect number 2. It is a common task in chemical and related industries to use octanol-water partition coefficients to aid in the design of product formulations with desired hydrophobicity or hydrophilicity character. ko/w is also used to estimate environmental bio-accumulation factors because it provides a crude model of partitioning between blood (water) and body tissue (1-octanol). Infinite-dilution activity coefficients are used to calculate air-water partition coefficients (Henry's Law constants) for environmental engineering applications. In addition, VLE of binary mixtures can be predicted (interpolated) over the entire binary composition using a two-parameter activity-coefficient model if the two infinite-dilution activity coefficients are known (Prausnitz, et.al, Molecular Thermodynamics of Fluid-Phase Equilibria, Third Edition, Appendix F, pps 804-807). Challenge: For each of the following molecules: (i) an amine [exact chemical formula censored] (ii) an alcohol [exact chemical formula censored] Compute the: (a) 1-octanol-water partition coefficient (mole-fraction units) at 300 K and 101.325 kPa. (b) Infinite-dilution activity coefficient (mole fraction units, Lewis and Randall reference state) for the organic molecule dilute in water at 325 K and 13.5 kPa.
Rules of the game:
Quantitative Accuracy Metrics (60%)
Relative Accuracy Metrics - Relative Ranking (40%): The computed octanol-water partition coefficient and the infinite-dilution activity coefficient of each molecule will be compared to the respective experimental values. The molecule that is in best agreement to experiment will be used as a normalization to determine relative coefficients (ie: (coefficient worst predicted)/(coefficient best)). The relative ratios will be compared to the corresponding normalized ratios using the experimental data. The quantity (coefficient/coefficient-ref)predicted will receive full credit if it is within 5% of the corresponding quantity (coefficient/coefficient-ref)expt . As in the quantitative accuracy section, similar partial credit will be awarded on a sliding scale. Click on the link below to see the 5th Challenge Problem scoring sheet. Molecule Problem Scoring Spreadsheet (MS Excel file) Other entry guidelines:
FAQ
Q: Based on the results of the 4th challenge, why not focus on vapor phase viscosity (which would represent a major methodological advance)?
A: While it does present some issues from a computation standpoint, it is not a property that had great industrial importance. When needed, other methods are available that give reasonably good estimates for vapor viscosity.
Q: Why not have a bigger scope by including a larger list of molecules covering a range of functionalities?
A: to be added
Q: Partitioning between octanol and water is complicated by the fact that water is soluble in octanol at a level of 0.2 to 0.3 in terms of mole fractions. Must entrants take this into account explicitly? Do they have to calculate the water saturation? Can they just ignore this complication?
A: to be added
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