2014
DOI: 10.1063/1.4883718
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Three-body interactions in complex fluids: Virial coefficients from simulation finite-size effects

Abstract: A simulation technique is described for quantifying the contribution of three-body interactions to the thermodynamical properties of coarse-grained representations of complex fluids. The method is based on comparing the third virial coefficient B3 for a complex fluid with that of an approximate coarse-grained model described by a pair potential. To obtain B3 we introduce a new technique which expresses its value in terms of the measured volume-dependent asymptote of a certain structural function. The strategy … Show more

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Cited by 20 publications
(41 citation statements)
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References 73 publications
(85 reference statements)
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“…3 of Ref. 27. We observe that the impact of three-and four- Notwithstanding the results displayed in Figs.…”
Section: A Similar Conclusion Can Be Drawn From Bsupporting
confidence: 54%
“…3 of Ref. 27. We observe that the impact of three-and four- Notwithstanding the results displayed in Figs.…”
Section: A Similar Conclusion Can Be Drawn From Bsupporting
confidence: 54%
“…35,52,53 The method will allow analysis of phase behaviour in these systems, and also quantification of the effects of manybody interactions. 34 Similar questions arises in systems where the large particles are not spherical, in which case the depletion interaction has a more complicated charac-ter [54][55][56] and can lead to new phase behaviour. 55,57 There are also potential applications of the TL method to other soft matter systems including star polymers and dendrimers, for which accurate coarse-grained models are available, 1,58,59 and whose phase behaviour is rich and complex.…”
Section: Discussionmentioning
confidence: 94%
“…For the second term on the right hand side of (D4), one uses (20,34,41) to show that |Ê| ≤ a. Hence | Ê 1 {2( +1)≤1} | ≤ a Prob( ≤ −1/2).…”
Section: Appendix D: the Bias Of The Estimatorâmentioning
confidence: 99%
“…If q < q 0 , the general relationship between the reservoir packing fraction η (r) s (or, equivalently, the fugacity z s ) and the values η s and η l of the binary mixture is derived in Appendix C with the result 20) where g eff (r|η l , η (r) s ) is the radial distribution function of a pure fluid of large particles interacting via the effective …”
Section: The Sao Modelmentioning
confidence: 99%