THE JOURNAL OF CHEMICAL PHYSICS 135, 204706 (2011) Constructing a new closure theory based on the third-order Ornstein-Zernike equation and a study of the adsorption of simple fluids Lloyd L. Leea) Department of Chemical and Materials Engineering, California State University, Pomona, California 91768, USA (Received 23 August 2011; accepted 2 November 2011; published online 30 November 2011) The third-order Ornstein-Zernike equation (OZ3) is used in the construction of a bridge functional that improves over conventional liquid-theory closures (for example, the hypernetted chain or the Percus-Yevick equations). The OZ3 connects the triplet direct correlation C(3) to the triplet total correlation h(3) . By invoking the convolution approximation of Jackson and Feenberg, we are able to express the third-order bridge function B3 as a functional of the indirect correlation γ . The resulting expression is generalized to higher-order bridge terms. This new closure is tested on the adsorption of Lennard-Jones fluid on planar hard surfaces by calculating the density profiles and comparing with Monte Carlo simulations. Particular attention is paid to the cases where molecular depletion on the substrate is evident. The results prove to be highly accurate and improve over conventional closures. © 2011 American Institute of Physics. [doi:10.1063/1.3663221] I. INTRODUCTION For fluids adsorbed on a solid surface, either of two situations may occur: (a) the value of the contact density is higher than the bulk density. There is a surplus of molecules at the wall. We call this adhesion. Or (b) the contact density is lower than the bulk value. Thus, there is a deficit of molecules at the wall. We call this depletion. There may also be the third possibility of an even distribution. In statistical mechanics, the density profile near and not far from the wall is described by the singlet probability density ρ w (z) (z being the distance normal to the wall). Far from the wall, ρ w approaches the constant bulk density value ρ 0 . Adhesion or depletion is a general behavior, present at either supercritical or subcritical states, with different substrate affinities, molecular species, and geometries of the inhomogeneities. Accumulation or detachment of molecules at the interface is the result of competition between the interfacial wall forces and the coherent fluid-fluid forces on the fluid molecules vis-à-vis the state conditions (phase diagrams, pressures, and temperatures) (see reviews of Refs. 1 and 2). On a planar hard wall this can be clearly shown by the well-known sum rule for the contact density ρ w (zc ): P0 , (1.1) kT where subscript “w” denotes properties under the influence of a wall potential w, and “0” denotes the bulk fluid property (at zero wall potential, i.e., w = 0). P0 is the bulk pressure, k is the Boltzmann constant, T is the absolute temperature, and zc is the contact distance of an adsorbate molecule. Therefore, if we know the fluid equation of state (EOS) ahead of time we can determine if we have fluid adhesion/depletion at the given temperature T and density ρ 0 . As an example, for the Lennard-Jones (LJ) fluid we know an EOS due to Nicolas ρw (zc ) = a) Electronic mail: [email protected]. 0021-9606/2011/135(20)/204706/11/$30.00 et al.3 For LJ fluid adsorbed on a hard planar wall (LJ/HW), at temperature, say, T* = kT/ε = 1.35 (ε is the LJ energy parameter), we can calculate ρ w (zc ) values at different bulk pressures P0 according to the sum rule equation (1.1). While from the EOS, we can also calculate the actual bulk densities ρ 0 that give rise to these pressures P0 . If we plot ρ w (1) (zc ) vs. ρ 0 (at the same P0 ) as in Fig. 1, ρ w (zc ) can be either higher than ρ 0 (higher contact value means adhesion) or lower than ρ 0 (lower contact value means depletion). A diagonal line marks off the two regions. Thus, the ρ 0 -axis is divided into two halfplanes: one half for depletion (in this case the left panel with lower densities) and the other for adhesion (the right panel at higher densities). The line of demarcation of the two at this temperature is at about ρ 0 * = ρ 0 σ 3 ∼ 0.66 (σ is the LJ size parameter). The precise value depends on the accuracy of the Nocolas EOS, which was first obtained from an empirical fit to the simulation data. In the LJ case, adhesion happens at high densities (ρ 0 * > 0.66), and depletion happens at low densities (ρ 0 * < 0.66). Of course, at a different temperature, the line might shift and the regions might multiply; and we shall have a different demarcation. Note that the isotherm T* = 1.35 is slightly supercritical for the LJ fluid (T* c,LJ ∼ 1.317). Density functional theories4 (DFT) have been employed to describe the adsorption behavior. There are several approaches in DFT: for example, the weighted-density approach (e.g., the fundamental measure theory5–8 ), the squaregradient approach,9, 10 and the perturbation/closure-based approaches11–14 (see reviews of Refs. 15–18). Historically, the closure-based theories (e.g., the wall-particle OrnsteinZernike (WOZ) integral equation approach19, 20 and its variations) were developed in the 1970s and were found to treat simple systems with adhesive behavior quite well; but did not always give quantitative answers for those cases with severe depletion.21–23 The closures used in these works were from the common uniform fluid theories, such as the 135, 204706-1 © 2011 American Institute of Physics Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-2 Lloyd L. Lee J. Chem. Phys. 135, 204706 (2011) 1.0 1.4 0.9 0.8 Adhesion Depletion HNC 0.7 1.0 0.6 ρw Contact density, ρ w 1.2 0.8 0.5 0.4 0.6 0.3 Diagonal PY 0.4 0.2 0.2 0.1 0.0 0.0 0.5 0.0 0.2 0.4 0.6 0.8 MC z 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 5.5 1.0 Bulk density, ρ 0 FIG. 1. Determination of the “depletion” and “adhesion” regions of adsorption for the Lennard Jones fluid on hard wall at T* = 1.35. The hard wall sum rule Eq. (1.1) is used to calculate the contact density ρ w at a given bulk pressure P0 . The bulk density ρ 0 at the same pressure P0 is obtained from an equation of state (Nicolas et al.3 ). A diagonal line (where ρ w = ρ 0 ) is used to divide the abscissa into two regions where ρ w < ρ 0 (depletion) or ρ w > ρ 0 (adhesion). Percus-Yevick24 (PY) closure (see below, Eq. (3.2)) or the hypernetted chain25, 26 (HNC) closure (Eq. (3.1)). Note that we have shown earlier27 that the WOZ approach19, 20 and the closure-based DFT (Refs. 11–14) are theoretically equivalent. Recently, there have been notable advances in the closurebased DFT.11–14, 28 Applications were made to various fluids (Lennard-Jones, Yukawa, and soft matters) and geometries (planar surfaces, parallel slits, spherical cavities). More sophisticated closures have been applied.11–14, 28 One can however pose the question: were the noted inadequacies of the WOZ for depletion adsorption due to the inherent errors in the approximate closure relations used (as found in the PY or HNC equations)? If so, can we improve the performance by correcting the errors and incorporating more fundamental physical principles that had been neglected earlier? In this work, we shall examine this question. We shall formulate a new closure theory based on the third-order Ornstein-Zernike (OZ3) equation (see below) and as a partial check of its validity apply it to the LJ/HW system, especially for cases of depletive adsorption. For LJ/HW, Balabanic et al.29 and Lutsko30 have provided Monte Carlo (MC) simulation data at T* = 1.35 and ρ 0 * = 0.50. The singlet density profile (symbol = diamonds) is shown in Fig. 2. Near the wall (zc = 0.5 σ ) the contact density ρ w (zc )σ 3 ∼ 0.2, while the bulk density is much higher ρ 0 * = 0.50. Thus, this case belongs to the depletion region. However, if we solve the Euler-Lagrange equation (see below, Eq. (1.4)) for the density profile with the PY and/or the HNC closure, we would obtain the two top curves shown in Fig. 2. They are overly oscillatory, and yield contact values that are too high. None of the closures (PY or HNC) shows any depletion (contact densities > 0.50). These two classical closures, successful for uniform fluids, are clearly not appropriate for the nonuniform LJ/HW system. The question is what is missing in PY and HNC that caused their poor performance for these nonuniform cases? FIG. 2. The singlet density profile ρ w(z) for LJ/HW system at ρ * = 0.5 (T* = 1.25). Diamonds = Monte Carlo data from Balabanic et al.22 Upper line = HNC closure. Lower line = PY closure. PY and HNC fail to give quantitative predictions of the MC ρ w (z). To establish nomenclature, we briefly review the commonly employed density functional theory based on the grand potential, . It is defined for a nonuniform fluid with an ex ternal potential w(r ) as ≡ F [ρw ] + d rρw (r )[w(r ) − μ0 ], where F is the intrinsic Helmholtz free energy functional, being a functional of ρ w (r ), and ρ w (r ) is the singlet density. μ0 is the chemical potential of the bulk fluid. Subscript w indicates nonuniform properties (in the presence of the wall potential w(r )), while subscript 0 indicates uniform properties (when the wall potential is zero, w = 0). The grand potential is minimized at the equilibrium singlet density and the EulerLagrange (EL) relation for this minimization is − δβF [ρ] = βw(r) − βμ0 = Cw(1) (r) − ln[ρw (r)3 ], δρw (r) (1.2) where β is the reciprocal temperature 1/(kT), k is the Boltzmann constant, T is the absolute temperature, and is the de Broglie wavelength. Rearrangements give (1.3) r ) − C (1) ρw (r ) = ρ0 exp − βw(r ) + C (1) w ( 0 . We have shown earlier27 that an equivalent form of the EL can be written as ρw (r ) = ρ0 exp − βw(r ) + γ w (r ) + Bw (r ) , (1.4) where Bw is the bridge functional in the presence of the external potential w. Comparing Eqs. (1.3) and (1.4) gives r ) − C (1) r ) + Bw (r ). C (1) w ( 0 = γ w ( (1.5) The nonuniform indirect correlation function (icf) γ w (r ) is defined, by analogy with uniform fluids, as γ w (r ) ≡ d r C0(2) (|r − r |)δρ w (r ), (1.6) where δρ w (r ) ≡[ρ w (r ) – ρ 0 ] ≡ ρ 0 hw (r ). hw is the nonuniform total correlation function. γ w (r ) as defined is a wallparticle correlation (not a particle-particle correlation). Note that the kernel in Eq. (1.6) is the uniform fluid pair direct correlation, C0 (2) . In this study, we shall re-examine the general basis of the closure relation for both nonuniform and uniform fluids. Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-3 Closure and the third-order OZ relation J. Chem. Phys. 135, 204706 (2011) We start by examining the triplet function C(3) (i.e., the triplet direct correlation function, DCF-3) based on the third order Ornstein-Zernike equations (Sec. II). OZ3 is an exact equation connecting the DCF-3 C(3) to the triplet total correlation function (TCF-3), h(3) . It allows interchange of expressions either in C(3) or in h(3) . Thus, we are able to express in closed form the third-order bridge function term B3 (see the Appendix and Sec. II) in terms of either C(3) or h(3) . By making appropriate approximations to the TCF-3 h(3) , we are able to construct a new and improved closure for the bridge functional for nonuniform fluids (Sec. III). In numerical implementation of the theory, we also visit the issue of renormalization of the base function used in the closure (Sec. IV). Tests on the LJ/HW systems are made (Sec. IV) and new and more accurate predictions are obtained for the “depletion” cases of adsorption. Conclusions and anticipated future directions are given in Sec. V. II. THE THIRD-ORDER ORNSTEIN-ZERNIKE EQUATIONS We have shown earlier31 that there are four members of the OZ3, based on the methods of Lebowitz and Percus32 on the functional derivatives. It is a generalization of the secondorder OZ2: (2) ( r , r ) − C (| r , r ) ≡ d r C0(2) (r , r )ρ 0 h(2) r , r ). h(2) 0 0 0 ( (2.1) As is known,32 Eq. (2.1) can be derived via the inverse matrix relation between the functional derivative δρ w (1)/δW(2) and its inverse δW(2)/δρ w (1), where W is the intrinsic chemical potential defined by W(r )≡βμ0 – βw(r ) (notation: arguments 1 = r1 and 2 = r2 , etc.): δρw (1) δW (3) = δ3 (1, 2), d3 (2.2) δW (3) δρw (2) where δ 3 (1,2) is the three-dimensional Dirac delta function δ 3 (r1 – r2 ). The functional derivatives are given explicitly by32 δρw (1) = δ3 (1, 2)ρw (1) + F (2) (1, 2), δW (2) and δ3 (1, 2) δW (1) = − C (2) (1, 2), δρw (2) ρw (1) (2.3) where F(2) is the Ursell distribution. OZ3 follows a similar pattern based on higher order functional derivatives, for example, δ 2 ρ w (1)/[δW(2)δW(3)]. OZ3 has four alternative forms, because one can choose different combinations of the partial differentials. We retrieve one of the forms31–33 explicit in C(3) (we shall drop the superscripts and subscript “w” to save space): C123 = h123 − C12 C13 − C21 C23 − C31 C32 3 2 −ρ d4d5d6 C14 C25 C36 h456 +ρ d5d6 C15 C26 h356 −ρ d5 C15 h235 + ρ 2 d4d5 C15 C34 h245 −ρ d6 C26 h136 + ρ 2 −ρ d4d6 C26 C34 h146 d4 C34 h124 + 2ρ d4 C14 C24 C34 (OZ3). (2.4) This equation is exact, since it is based on the following exact inverse matrix relation:32 δ 2 W (1) δW (4) δW (6) δW (1) = − d4d5d6 δρw (2)δρw (3) δρw (3) δρw (2) δρw (5) × δ 2 ρw (5) . δW (4)δW (6) (2.5) The notation is self-explanatory: i.e., C12 = C(2) (1,2), C123 = C(3) (1,2,3), and h12 = h(2) (1,2), h123 = h(3) (1,2,3), etc. We observe that C(3) necessarily involves the triplet TCF h(3) in convolution with pair correlations. If we know h(3) , we can calculate C(3) (vice versa). The knowledge of C(3) will impact on the closure relations. A. Closure theories A closure expresses the bridge function B(r) in terms of a function B̂(γ ), or in terms of a functional B[γ (r)], of an argument function γ (r), i.e., equations postulated between the bridge function B and other known liquid-theoretical correlation functions (such functions can, in different approximations, be the thermal potential ω, the cavity function y, and/or the indirect correlation γ ). Most existing closure equations are approximate in one way or another because they make plausible simplifications to the exact relation (which is a functional). In statistical mechanics, the bridge function B(r) itself is a formally defined quantity: either as an infinite cluster series34 or as a functional Taylor expansion.35 However, direct numerical evaluation from these definitions is extremely cumbersome if not impossible (due to the infinite number of terms and lack of knowledge of high-order correlations). Thus, truncations were made entailing questionable convergence problem. On the other hand, with computer simulations, the bridge function B(r) can be inverted directly from the simulation data based on its definition (see Eq. (2.6) below). This type of reverse engineering (i.e., inversion from the machine data) has been done many times before.36 The definition of Bw is (we shall switch back to the nonuniform Bw from the uniform B without loss of validity) Bw (r ) ≡ ln yw (r ) − γw (r ), (2.6) which is in fact a rearrangement of the Euler-Lagrange equation (1.4). The cavity function yw is defined as ln[yw (r )] ≡ ln[ρ w (r )/ρ 0 ] + βw(r ). We, equipped with the simulated density distributions h(2) (r) or ρ w (r ) (from MC or molecular dynamics (MD)), can obtain γ (r) = h(2) (r) – C(2) (r) from Eq. (2.1) (in the homogeneous case) or γ w (r ) from Eq. (1.6) (in the inhomogeneous case). With MC inputs to the righthand side of Eq. (2.6), the bridge function Bw (r ) can be calculated. This raw data-inverted bridge function has been determined earlier and reported for the LJ/HW system in Ref. 27. For the state of ρ * = 0.50 (T* = 1.35), the Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-4 Lloyd L. Lee J. Chem. Phys. 135, 204706 (2011) 2 1.5 1 w 0.5 Z 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 Since we have derived, from OZ3, the exact expression for C(3) , it is a simple matter to substitute Eq. (2.4) into Eq. (2.8) (the full result is given in the Appendix). We have at hand an exact expression (A1) for B3 in terms of h(3) . However, the final equation is not amenable to numerical calculations because of the lack of knowledge of the triplet TCF h(3) . We shall thus consider making “approximations” to h(3) . -0.5 -1 -1.5 III. CONSTRUCTION OF A CLOSURE THEORY BASED ON HIGHER-ORDER OZ RELATIONS B w -2 -2.5 FIG. 3. The nonuniform bridge function Bw (z) (lower line) at ρ * = 0.50 as obtained from inversion of the MC data39 according to the definition (2.6). Also shown is the MC- inverted indirect correlation γ w (z) (Eq. (1.6), upper line). Both are derived from the MC data, without any approximation. bridge function Bw (z) is depicted in Fig. 3 (where we have also shown the MC-inverted icf γ w (z)). Thus, the bridge function Bw (r ) as a function of r “exists” for nonuniform fluids, contrary to speculations otherwise. The next question is whether this curve (in Fig. 3) is related (based on distribution theory) to other well-known correlations (beyond the definition (2.6))? The relation Bw = B̂ w (γ ), if it exists, is called a closure (the name was originally derived from the complementary relation supplied in order to “close” the OZ2 equation (2.1), to make it solvable). It constitutes a liquid-state theory that is the crux of the matter in establishing a closurebased DFT. We reiterate: the bridge function Bw (r ) is a welldefined function of rand it exists (as defined by Eq. (2.6)) and is obtainable by numerical inversion of simulation data; while a closure relation Bw = B̂ w (γ ) is an equation (theory) between this bridge function and other correlation functions. This equation is, generally speaking, a functional Bw = Bw [γ ]. In few instances, the functional may reduce to a function B̂ w (γ ) (caret means a function of another “argument function,” the argument function is here γ = γ (r )). The bridge function can be expanded in functional Taylor series (with the uniform system as the reference) (see, e.g., Ref. 27): 1 d2d3 C0(3) (1, 2, 3)δρw (2)δρw (3) Bw (1) ≡ 2! 1 + d2d3d4 C0(4) (1, 2, 3, 4)δρw (2)δρw (3)δρw (4) 3! 1 + d2d3d4d5 C0(5) (1, 2, 3, 4, 5)δρw (2)δρw (3)δρw 4! 1 1 ··· + + ··· 5! 6! = B3 + B4 + B5 + B6 + · · · , respectively. × (4)δρw (5) + (2.7) In the last equality, we have used the order of the DCFs to define the abbreviations B3 , B4 , and higher order terms. For example, the third-order term B3 is given by 1 B3 (1) ≡ d2d3 C0(3) (1, 2, 3)δρw (2)δρw (3). (2.8) 2! In this section, we shall discuss some of the possible simplifications that can be made to h(3) in Eq. (2.4). This is for the purpose of constructing a usable closure theory. The simplification cannot be too simple so as to lose accuracy, and not too complicated to be unwieldy. We shall zero in on one specific approximation and analyze its role in the formulation of future closure equations. We shall also analyze some of the commonly known closures (such as PY and HNC) in light of OZ3. The simplest approximation, which has been proposed for B, is to set C(3) as well as all higher order terms C(n) (n > 3) to zero (or set their weighted integrals to zero). This in essence is the Ramakrishnan-Yussouff theory37 in DFT (or the hypernetted-chain equation): C (3) (1, 2, 3) ∼ = 0, (HNC). (3.1) A more judicious policy may be to select appropriate approximations to the triplet h(3) that appears in Eq. (2.4). We aim at simplifying Eq. (2.4) while preserving as much physics as possible in C(3) (and subsequently in B3 ). Several options are examined below. (We shall drop the subscript “w” without ambiguity owing to the isomorphism between the expressions of nonuniform and uniform quantities, especially in light of the Percus test-particle trick.38 ) First, the common PY closure can be expanded 1 1 B̂(γ ) = ln(1 + γ ) − γ = − γ 2 + γ 3 2 3 1 − γ 4 + − · · · , (PY). (3.2) 4 To decipher the specific terms in the expansion (3.2), we compare the terms with the exact expression (2.7). For B3 , we can match the γ 2 -terms from Eqs. (2.8) and (3.2) by making the specific approximation (3.4) below to C(3) : 1 B3 (1) = d2d3 C0(3) (1, 2, 3)δρw (2)δρw (3) 2! 1 ∼ d2d3 C0(2) (1, 2)C0(2) (1, 3)δρw (2)δρw (3) =− 2! 1 = − γ (1)2 , 2 where we have set C (3) (1, 2, 3) ∼ = −C (2) (1, 2)C (2) (1, 3), (PY). (3.3) (3.4) Observations are as follows: (i) approximation (3.4) in PY is a fragment of the exact OZ3 expression (2.4). We can identify the term −C(2) (1, 2)C(2) (1, 3) in Eq. (2.4). (ii) Equation (3.4) misses many terms and, in particular, two other product terms Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-5 Closure and the third-order OZ relation J. Chem. Phys. 135, 204706 (2011) C(2) C(2) , thus becoming “asymmetric” in the indices 1, 2, and 3 (symmetry is a necessary condition for a correct C(3) ). These are obvious “defects” in the PY theory, as revealed by examining the B3 term. We expect more deficiencies in PY coming from higher order terms. Other choice approximations to the triplet h(3) include (i) the convolution approximation (CA) of Jackson and Feenberg,39 (ii) the Kirkwood superposition (KS),40 and (iii) others. The convolution approximation was proposed for calculating the matrix elements of the phonon-phonon interactions in quantum fluid:39 convolution approximation equation (3.5), by switching the roles of h(3) and C(3) . (iii) This formula improves over the Percus-Yevick formula (3.4) by symmetrizing the arguments with three product terms and including a convolution integral. We shall call (3.7b) the CA-C3 approximation. In cluster diagrams we can see the “symmetry” of terms C(3) (1, 2, 3)(CA-C3) = h(3) (1, 2, 3) ∼ = h(2) (1, 2)h(2) (1, 3) + h(2) (2, 1)h(2) (2, 3) + h(2) (3, 2)h(2) (3, 1) +ρ d4 h(2) × (1, 4)h(2) (2, 4)h(2) (3, 4) (CA-h3). (3.7c) (3.5) After some algebra, it turns out that Eq. (3.5) implies also that C(3) = 0, similar to the HNC approximation. We shall call the Jackson-Feenberg equation (3.5) the CA-h3 approximation. The Kirkwood superposition40 is given by g (3) (1, 2, 3) ∼ = g (2) (1, 2)g (2) (1, 3)g (2) (2, 3). (3.6a) By applying the definitions of h(3) and g(3) , we obtain h(3) (1, 2, 3) ∼ = h(2) (1, 2)h(2) (1, 3) + h(2) (2, 1)h(2) (2, 3) + h(2) (3, 2)h(2) (3, 1) + h(2) (1, 2)h(2) (2, 3)h(2) (3, 1) (Kirkwood). (3.6b) Comparing Eqs. (3.5) and (3.6b), we see that the two equations are similar except that the convolution integral (last term in Eq. (3.5)) is replaced by the cyclic product in Eq. (3.6b). The expression of KS-based C(3) can be easily obtained by substitution of Eq. (3.6b) into Eq. (2.4) (details not shown). Abe41 and Salpeter42 have further extended KS to higher order terms. Bildstein et al.43 have analyzed the performance of Eq. (3.6b) for h(3) . Aside from these common formulations, other approximations can be made for h(3) . Following the example of Jackson and Feenberg,39 we also propose a convolution approximation but with a variation: instead of setting C(3) = 0 as Jackson and Feenberg did, we set h (1, 2, 3) ∼ = 0. (3) (3.7a) Thus, Eq. (2.4) simplifies to C (3) (1, 2, 3) ∼ = −C (2) (1, 2)C (2) (1, 3) − C (2) (2, 1)C (2) (2, 3) − C (2) (3, 2)C (2) (3, 1) +2ρ d4 × C (2) (1, 4)C (2) (2, 4)C (2) (3, 4) (CA-C3). (3.7b) (i)This expression is “symmetric” in its arguments (i.e., it maintains permutation invariance in 1, 2, and 3). (ii) This is a counterpart, in mirror image, of the Jackson-Feenberg (where a single bond represents the C(2) function; filled circle is an integrated field point). The ansatz h(3) = 0 may seem unjustified. However, after propagation through the OZ3 equation (2.4), the value of the outcome remains to be weighed. Just as the assumption, C(3) = 0, seemed contrived at first, the effect of the JacksonFeenberg equation is quite salutary for quantum fluid. It was pointed39 out that the convolution approximation satisfies the recursion and normalization conditions of the distribution functions, while the Kirkwood superposition does not. We shall reserve judgment on CA-C3 before it has a chance of being fully tested. The third choice is the triple product formula due to Barrat, Hansen, and Pastore (BHP):44 C (3) (1, 2, 3) ∼ = t(1, 2)t(2, 3)t(3, 2), (3.8) where t(1,2) is an unknown function and is to be determined by the sum rule on the derivatives of DCF. The validity of Eq. (3.8) has been investigated in Ref. 44. The validity of Eq. (3.7b) has been shown partly in Ref. 45. Other approximations exist in literature,46–56 and the promising ones will be investigated. A. Implications of the convolution approximation on the B3-term We substitute the CA-C3 expression (3.7b) into Eq. (2.8) for B3 and obtain after some algebra γ (1, 2)2 − ρ d3 C (2) (1, 3)h(2) (3, 2)γ (3, 2) B3 (1, 2) ∼ =− 2 + ρ d3 C (2) (1, 3)γ (3, 2)2 . (3.9) This equation expresses B3 both as a function and as a functional of the icf γ . Comparison of Eq. (3.9) with the PY expansion (3.2) shows that they share one common term – γ 2 /2. Equation (3.9) is obviously a correction to PY by including the two extra integrals. If Eq. (3.9) can be considered as an improvement over PY at order n = 3, what improvements shall come from the higher order terms (n > 3)? We formally Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-6 Lloyd L. Lee J. Chem. Phys. 135, 204706 (2011) consider the fourth-order Ornstein-Zernike equation (OZ4) below. B. Consideration of the OZ4 Formula The OZ4 equations31 can be obtained from the third functional derivatives of the form δ 3 (.)/δ(.)δ(.)δ(.) with differentials from the singlet densities ρ w and the intrinsic chemical potential W. There are six members of OZ4. One of the OZ4 members is derived from the following chain rule: − δ 3 W (1) δρw (2)δρw (3)δρw (4) · F3 (1, 2, 3) δ 2 ρw (6) δW (7) δW (1) δ 2 W (5) = d5d6d7 δρw (3) δρw (6) δρw (2)δρw (3) δW (5)δW (7) δ 2 ρw (6) δW (5) δW (1) δ 2 W (7) + d5d6d7 δρw (4) δρw (6) δρw (2)δρw (3) δW (5)δW (7) δ 2 ρw (6) δW (5) δW (7) δ 2 W (1) + d5d6d7 δρw (4) δρw (3) δρw (2)δρw (6) δW (5)δW (7) δW (5) δW (8) δW (7) δW (1) + d5d6d7d8 δρw (4) δρw (2) δρw (3) δρw (6) δ 3 ρw (6) . × δW (5)δW (7)δW (8) (3.10) After substituting the known formulas for the functional derivatives (see, e.g., Eq. (2.3)), Eq. (3.10) will give a lengthy expression involving C(4) and h(4) , plus integrals of lower order correlations. We shall not write out explicitly the details, except by noting that (i) it contains product terms of C(2)’ s which shall yield the γ 3 -term shown in PY equation (3.2); (ii) it will contain additional integrals of C(n) and h(n) with forms more or less similar to those in Eq. (2.4), except being lengthier. In principle, OZ4 can be used to obtain the exact term B4 in the bridge function (2.7). We would have traded B4 as a function in C(4) to a function in h(4) . Unless we already knew h(4) , the exercise is not of much practical utility. Thus, instead, we shall consider, in the following, a resummation scheme. C. Resummation of the higher-order bridge terms We start with the BHP (Ref. 44) formula (3.8). We notice that in Ref. 44, the t-function obtained resembles in many ways, in shape and in range, to the pair DCF C(2) (see Fig. 1 in Ref. 44, 1988). We conjecture that a superposition of three pair DCF’s C(2) would probably be equally as effective. Namely (k being a constant to be determined), C (3) (123) ≡ kC (2) (12)C (2) (13)C (2) (23), (3.11) or more generally, by applying a “modification” function F3 (1,2,3) such that C (123) ≡ C (12)C (23)F3 (1, 2, 3), (3) (2) sented before.57 We shall include here for completeness. We examine the B3 term: ρ2 B3 (10) ≡ d2d3 C (3) (123)h(20)h(30) 2! ρ2 = d2d3 F3 (1,2,3)[C (2) (12)h(20)] [C (2) (13)h(30)] 2! ρ2 = d2 [C (2) (12)h(20)] · d3 [C (2) (13)h(30)] 2! (2) (3.12) F3 (1,2,3) is considered as defined by Eq. (3.12) in terms of C(3) and C(2) . Certainly, F3 (1,2,3) must be such that it satisfies the symmetry requirements of C(3) (invariant under permutations of the three arguments 1, 2, and 3). With this definition of F3 , we shall develop a resummation formula for the bridge function. Some of these arguments have been pre- = (apply mean-value theorem to F3 ) 1 1 F̄3 [h(10) − C (2) (10)]2 = F̄3 γ 2 (10). (3.13) 2! 2! To make progress, we have applied the mean-value theorem to F3 (1,2,3) in the last equality. This gives a mean valueF̄3 . We have also used the OZ relation (2.1) for the convolution of h(r) and C(r) to obtain the icf γ (r). Similarly, we factorize C(4) in terms of an F4 (1,2,3,4) function: = C (4) (1234) ≡ C (2) (12)C (2) (13)C (2) (14)F4 (1, 2, 3, 4). (3.14) Applying the mean value theorem to F4 (1,2,3,4), the fourthorder term in Eq. (2.7) becomes ρ3 B4 (10) ≡ d2d3d4 C (4) (1234)h(20)h(30)h(40) 3! ρ3 = d2d3d4 F4 (1, 2, 3, 4) [C (2) (12)h(20)] 3! × [C (2) (13)h(30)] [C (2) (14)h(40)] (apply mean-value theorem to F4 ) 1 1 F̄4 [h(10) − c(2) (10)]3 = F̄4 γ 3 (10). (3.15) 3! 3! Repeated applications of the modification functions Fn to higher order C(n) s, and applications of the mean value theorem result in the infinite series = B(10) ≡ B(r) ≡ F̄3 2 F̄4 F̄5 γ (10) + γ 3 (10) + γ 4 (10) + . . . , 2! 3! 4! F̄3 2 F̄4 F̄5 γ (r) + γ 3 (r) + γ 4 (r) + · · · . 2! 3! 4! or (3.16) The mean valuesF̄3 , F̄4 , . . . are now functions of T and ρ; and r = |r0 – r 1 | is the inter-particle distance. Let us examine the PY expansion (3.2). Matching terms of Eq. (3.2) with Eq. (3.16) give the mean values F̄i for PY: F̄3 = −1, F̄4 = 2, F̄5 = −6, . . . etc. (PY). (3.17) Thus, in the PY approximation, the mean values F̄i are constants, independent of the state condition. As to the Verlet closure58 (α being a constant = 0.8) γ2 2(1 + αγ ) γ2 = − [1 − αγ + α 2 γ 2 − α 3 γ 3 + α 4 γ 4 − + · · ·] 2 (Verlet). (3.18a) B̂(r) ∼ =− Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-7 Closure and the third-order OZ relation J. Chem. Phys. 135, 204706 (2011) Comparison with Eq. (3.16) gives F̄3 = −1, F̄4 = 3α, F̄5 = −12α , . . . etc. (Verlet). 2 (3.18b) It is obvious that the expansion of Verlet differs from the PY closure. Verlet’s closure has been shown to be far superior, for hard spheres, to the PY closure. Another closure of interest is the so-called ZSEP closure59, 60 (the zero-separation closure, i.e., a closure that satisfies the zero-separation theorems for the cavity functions) (α, ϕ, and ζ are adjustable parameters and are functions of T and ρ. They can be determined by enforcing the thermodynamic consistencies.): ζ 2 φ ∼ B̂ZSEP (r) = − γ (r) 1 − φ + . 2 1 + αγ (r) =− γ2 ζ [1 − φαγ + φα 2 γ 2 − φα 3 γ 3 + − . . .] 2 (ZSEP). (3.19) This closure reduces to the Verlet closure upon taking ϕ = 1 and ζ = 1. Comparison with Eq. (3.16) gives the following interpretation of the mean values: F̄3 = −ζ, F̄4 = 3αφζ, F̄5 = −12α 2 φζ, . . . etc. (ZSEP). (3.20) We shall adopt this ZSEP form as one part of the resummation formula for B (the part that is a function of γ , see Eq. (3.9). For the other parts involving the integrals (i.e., as a functional of γ in Eq. (3.9)), we shall retain the same format of the integrals while adding a multiplicative factor ψ in order to modulate their values so as to include higher order contributions. The justifications are based on the following assumptions: (i) the B-expansion (2.7) is fast convergent after the third-order term n > 3; (ii) the modification Fn -function expansion does not include all high-order effects, thus the residual is to be accounted for by the convolution integrals in Eq. (3.9); and (iii) the higher-order integrals can scale proportionally as the third-order integrals in Eq. (3.9). The final resummed form we propose is φ ζ γ (1, 2)2 1−φ+ B(1, 2) ∼ =− 2 1 + αγ (1, 2) − ψρ d3 C (2) (1, 3)h(2) (3, 2)γ (3, 2) + ψρ (2) d3 C (1, 3)γ (3, 2) 2 (CA-OZ3). (3.21) This closure relation (3.21) will be called CA-OZ3 (the convolution approximation-based OZ3). Written out for nonuniform fluids, φ ζ γw (r )2 1−φ+ . Bw (r ) = − 2 1 + αγw (r ) + ψρ0 d r C0(2) (|r − r |)γw (r )[γw (r ) − hw (r )] (CA-OZ3). (3.22) We shall choose this CA-OZ3 equation (3.22) as the test closure in this work. Other sophisticated schemes of approximation to h(3) , as discussed earlier or found in literature,46–56 can be developed along the same line and will be taken up at a later date. IV. NUMERICAL CALCULATION FOR THE LENNARD-JONES FLUID/HARD WALL SYSTEM The Lennard-Jones fluid/hard wall system has been extensively studied in the literature.30, 61, 62 The fluid-fluid potential is u(r) = 4ε [(σ /r)12 – (σ /r)6 ] (ε is the energy parameter and σ is the size parameter). Balabanic et al.29 and Lutsko 30 have carried out MC simulations for the singlet density profiles at T* = 1.35 and the three densities ρ * = (i) 0.50, (ii) 0.65, and (iii) 0.82. At these densities, judging from the chart presented in Fig. 1, cases (i) and (ii) belong to “depletion” adsorption, while case (iii) belongs to “adhesion” adsorption. We have shown earlier27, 63 that at ρ * = 0.82 (the adhesion case), the density profile ρ w (z) of MC is well reproduced by the ZSEP closure (Eq. (3.19)). See also Eq. (4.4) below). For the depletion cases (ρ * = 0.50 and 0.65), the ZSEP closure (3.19) is less successful (see Fig. 12 of Ref. 27). The present closure (4.22) is proposed to close this gap. In using Eq. (3.22), it is imperative that one “renormalizes” the argument function,59, 60, 64 i.e., changing the icf γ w in such a way as to extract out the long-range contributions. A. Renormalization of the base function γ w Instead of Eq. (1.6) for γ w which uses the bulk LennardJones pair DCF C0 (2) as the kernel (4.1) γ w (r ) ≡ d r C0(2) (|r − r )δρ w (r ), we construct a new base function γ H (r) (a renormalized function27 ) by using the short-range “core” part (i.e., CH (2) defined below) of C0 (2) to get (4.2) γ H (r ) ≡ d r CH(2) (|r − r )δρ w (r ), where CH(2) (r) ≡ C0(2) (r), for r ≤ σ ; and CH(2) (r) ≡ 0, for r > σ. (4.3) Namely, the renormalization takes the core part (r ≤ σ ) of the bulk DCF, and discards all function values of C0 (2) beyond the core. To illustrate the advantage of the core-based γ H , we renormalize the ZSEP closure (3.19) as 2 φ ζ γH (r)2 Renorm ∼ 1−φ+ BZSEP (r) = − . (4.4) 2 1 + αγH (r) We shall construct the Duh-Haymet65 plots for BZSEP (r) and γ H (r) (see Ref. 27). The MC data of Balabanic et al. were used to calculate (i) γ H according to Eq. (4.2) and (ii) the inverted bridge function according to Eq. (2.6). The DuhHaymet diagram is shown in Fig. 4 for the case ρ * = 0.65 (T* = 1.35). We observe that the curve for the pair Bw -γ H is a one-to-one function and well-behaved; while the curve Bw -γ w Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-8 Lloyd L. Lee J. Chem. Phys. 135, 204706 (2011) g0 2.5 0 -0.5 0 0.5 1 1.5 2 2.5 -1 3 3.5 4 4.5 5 γ 5.5 vs.γ H 2 1.5 Bw -2 -3 1 vs.γ w 0.5 r 0 0.5 1 1.5 2 2.5 3 3.5 4 -4 FIG. 4. The Duh-Haymet plot for Bw vs. γ w (lower curve) and Bw vs. γ H (upper curve) at ρ * = 0.65. The lower curve shows multiple function values and a strange “hook” near the origin. (un-renormalized) shows bizarre “kinks” with multiple function values. Bw -γ w does not satisfy mathematically the definition of a function (not single-valued). In other words, it is not possible to have a function relation between Bw and γ w (in fact, Bw is a functional, not a function, of γ w ). By extracting out the extra-functional contributions as was done with the base function γ H , Bw is made into a function Bw = B̂(γ H ). This is the advantage of using the Duh-Haymet plots for detecting function relationships. The above observations were derived entirely from MC data, no theories were used. The CA-OZ3 based closure (3.22) can now be written after renormalization as φ ζ γH (r )2 1−φ+ Bw (r ) = − 2 1 + αγH (r ) +ψρ0 d r CH(2) (|r − r |)γw (r ) ×[γw (r ) − hw (r )] (CA-OZ3 renormalized). (4.5) It contains four parameters α, ϕ, ζ , and ψ that are to be determined by known theoretical principles. One of the criteria chosen is the hard wall sum rule equation (1.1). At this rodage stage, we let the other three parameters float while using the MC data to guide the choice of their values (In the future, we shall use other known sum rules28, 66 to decide their values). To solve the EL equation (1.4) for the nonuniform density profiles, one needs as input the pure Lennard-Jones pair DCF C0 (2) . For T* = 1.35 and ρ * = 0.50, 0.65, and 0.82 we employed an accurate integral equation theory59, 60 (the ZSEP theory, Eq. (3.19)) to supply these inputs. To check the accuracy of the ZSEP results, we have carried out new molecular dynamics simulations for pure LJ fluid in this work. Since MD does not directly produce the direct correlation functions, we calculated instead the radial distribution functions (RDF) g(2) (r) for the three density states. (Note that the DCF can be obtained from the RDF through the OZ2 equation.) The theoretical ZSEP-calculated g(2) (r) are compared with the MDgenerated RDF. We verify that there is excellent agreement FIG. 5. Comparison of the radial distribution functions g0 (r) of the bulk (pure Lennard-Jones) fluid obtained from the ZSEP method (Eq. (3.19)), (the three lines) and the new molecular dynamics data (the symbols). This is for testing the accuracy of the ZSEP integral equation and, consequently, the bulk DCF values. Conditions: T* = 1.35 and ρ * = 0.50, 0.65, and 0.82. between the two (Fig. 5), lending credence to the DCF C0 (2) ’s used here. B. External potential, w(z) The hard wall external potential w(z) is taken to be σ σ w(z) = ∞, if z < ; and = 0, if z ≥ ; (4.6) 2 2 where σ is taken to be the same as the LJ size parameter. z is the distance of the center of a LJ molecule perpendicular to the wall. We shall use the LJ σ as the unit of length in the figures and in the following. C. Depletion adsorption of the Lennard-Jones fluid For density ρ * = 0.50, the parameters (α, ϕ, ζ , and ψ) determined are listed in Table I. The EL equation (1.4) was solved by numerical iterations using Picard’s method with relaxation.27 The grid size z = 0.005σ and the grid number N = 4096. This gave an integration range of 20.48 σ . For a number of cases, the range was doubled to 40.96 σ with 8192 grid points. Cauchy’s absolution convergence was checked with the γ w -function. Convergence criterion is δ = 0.00001. Double precision for all the variables was adopted. For details, see Ref. 27. Figure 6 shows six curves at the density ρ * = 0.50: the singlet densities ρ w (z): one from the CA-OZ3-based closure TABLE I. Parameters used in the CA-OZ3 closure (4.5) for the LJ/HW system at T* = 1.35. 2 Closure: Eq. (4.5) Bw (r ) = − ζ γH2(r ) 1 − φ + 1+αγφ (r ) H (2) +ψρ0 d r CH (|r − r |)γw (r )[γw (r ) − hw (r )] ρ* 0.50 0.65 0.82 α 2.0 5.0 0.51 φ 1.0 0.95 1.0 ζ 1.215 3.05866 0.87 Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp ψ 0.155 0.0079 0 204706-9 Closure and the third-order OZ relation J. Chem. Phys. 135, 204706 (2011) 3.5 5 γ 2.5 γ 1.5 0.5 ρ 4 γ 3 γ H H w 2 w ρ w 1 w 0 -0.5 0.5 1 1.5 2 B 2.5 w 3 3.5 4 4.5 5 5.5 6 6.5 7 7.5 8 Z -1.5 -1 0.5 1 1.5 2 2.5 3 3.5 4 4.5 z Bw -2 5 -3 -2.5 FIG. 6. Results of calculations with the new closure (CA-OZ3, Eq. (4.5)) at ρ * = 0.50. We show six curves: γ H = top curve; γ w = next lower curves; next three curves are for ρ w . They are (i) from CA-OZ3, (ii) from MC of Balabanic et al.,29 and (iii) from MC of Lutsko.30 These three curves are very close and indistinguishable at the scale shown. The lowest curve = Bw (obtained from the present closure CA-OZ3). (black line); and two curves from the two different sources of MC – (♦) = Lutzko30 and (×) = Balabanic29 ; the icf γ w (z) (un-renormalized, second curve from the top); the renormalized γ H (z) (the top curve); and the bridge function Bw (z) (the lowest curve). We notice that the renormalized γ H (z) is higher than the original γ w (z), as the core-valued CH (2) will enhance the function values. γ H (z) is also less oscillatory than γ w and stays mostly in the positive territory. The ρ w (z) values from CA-OZ3 and the two MC sources are indistinguishable on this scale. Figure 7 magnifies the y-axis. The density profile ρ w (z) from the CA-OZ3 matches closely the MC curves. The theoretical curve stays well within the statistical errors of the MC simulations. This agreement confirms that the new closure theory is successful for highly depleted absorption (in contrast to the PY and HNC theories (Fig. 2) where large deviations from the MC data were incurred). For density ρ * = 0.65, the state is near the border between depletion and adhesion (see Fig. 1). Examination of FIG. 8. Results of calculations with the new closure (CA-OZ3, Eq. (4.5)) at ρ * = 0.65. We show five curves: γ H = top curve; γ w = next lower curve; then two curves for ρ w : (i) from CA-OZ3 and (ii) from MC of Balabanic et al.29 The lowest curve = Bw (obtained from the present closure CA-OZ3). the MC density profile shows that there is some “depletion” taking place outside the wall (the location is shifted to a larger distance r ∼ 1.2σ ). At contact, ρ w (σ /2) is about 0.60 (compared to the bulk density of 0.65). So we have depletion. Conventional closure theories (PY or HNC) failed to give quantitative description for this case. We apply the CA-OZ3 closure to this state. The results are shown in Fig. 8 and the parameters used are listed in Table I. Five curves are given in Fig. 8: the CA-OZ3-calculated singlet density ρ w , the icf γ w , the renormalized γ H , the bridge function Bw , and the MC data ρ w .30 We witness again that the values of γ H are higher than γ w . The singlet density ρ w is well predicted by CA-OZ3. The last curve is blown up in Fig. 9. The CA-OZ3 curve shows a slightly “exaggerated” structure near the wall (between 0.6 < r* < 1.1), but settles down to the correct values at larger r. Overall, the agreement is excellent. D. Adhesive adsorption of the Lennard-Jones fluid For the first two cases with depletion (ρ * = 0.50 and 0.65), the CA-OZ3 is shown to perform accurately. For the 1 0.8 ρ 1.4 w 1.2 1 0.6 ρw 0.8 0.4 0.6 0.4 0.2 Z 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 5.5 6 6.5 7 7.5 8 FIG. 7. Enlarged view (from Fig. 6) of the singlet density ρ w (z) at ρ * = 0.50. Comparison of the new closure CA-OZ3 result with Monte Carlo data. Diamond = MC (Lutsko30 ); Cross = MC (Balabanic29 ); Line = CAOZ3 closure. 0.2 Z 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 FIG. 9. Enlarged view (from Fig. 8) of the singlet density ρ w (z) at ρ * = 0.65. Comparison of the new closure CA-OZ3 result with Monte Carlo data. Diamond = MC (Lutsko30 ); Cross = MC (Balabanic29 ); Line = CAOZ3 closure. Author complimentary copy. Redistribution subject to AIP license or copyright, see http://jcp.aip.org/jcp/copyright.jsp 204706-10 Lloyd L. Lee J. Chem. Phys. 135, 204706 (2011) tion equation:67 2.5 ∂σ = −, ∂μ 2 ρw 1.5 1 0.5 Z 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 FIG. 10. Comparison of the singlet density profile, ρ w (z), at ρ * = 0.82 from (i) Diamonds = MC (Balabanic29 ) (ii) Line = CA-OZ3 (or ZSEP) calculation. This is an “adhesion” case. adhesion adsorption at ρ * = 0.82, this is not a “difficult” case. Most closure-based DFT can give quantitative prediction for its profile. For completeness, we show in Fig. 10 the result of ρ w using the CA-OZ3 closure (4.5). The agreement is again very close at this high density. The parameters are given in Table I. V. CONCLUSIONS Starting from the exact relation of the third-order Ornstein-Zernike equation (2.4), we are able to formulate a viable approximation to the triplet direct correlation function C(3) in Eq. (3.7b) (the CA-C3). This approximation is modeled after the convolution approximation of Jackson and Feenberg. Substitution into the functional expansion of the bridge function (2.7) enables us to obtain in closed form an expression (3.9) for the third-order term B3 of the bridge function. Using the B3 equation as a basis, we generalize to a full closure equation (the CA-OZ3 equation (4.5)) for the bridge function. This CA-OZ3 equation is shown to be an improvement over the classical Percus-Yevick closure. The prominent difference is that it is at the same time a function and a functional of the indirect correlation function γ w , with convolution integrals involving also other correlation functions. We test this new closure by calculating the density profiles of the Lennard-Jones fluid adsorbed on a planar hard wall. The calculations prove successful in predicting the depletive adsorption cases as well as the adhesive adsorption. Traditionally, depletion has been treated by other density functional theories (such as the fundamental measure-based theories5–7, 61, 62 ). We show here by “updating” the closure equation with the aid of fundamental theories (in this case the OZ3), we can achieve improvements with the closure-based theories. As the formulation stands, the present approach is not self-contained. There are four parameters in the closure equation (4.5). To determine their values, we need at least four theoretical conditions to fix α, ϕ, ζ , and ψ. One of the conditions that has been used is the hard-wall sum rule (Eq. (1.1)). In future developments, we shall also use the Gibbs adsorp- (5.1) which links the surface tension σ to the adsorption density . In addition, the sum rules proposed by Henderson66 can be employed to ensure self-consistency. The CA-OZ3 formulation is only one of many other possible improvements. Other viable theories on the triplet correlations, some of which we have alluded to here, will be examined in the future. The positive outcome also opens the door to the study of a variety of other fluid systems (such as the Yukawa fluids, Coulomb fluids, and some of the soft matter potentials). Our derivations were based on “bulk fluid” (uniform system) statistical mechanics. However, we note that the closure relation proposed here can equally well be applied to nonuniform as well as uniform systems through Percus’ prescription of the source particles that puts the nonuniform fluids on equal footing with the uniform fluids.38 ACKNOWLEDGMENTS We are thankful to the OSCER Supercomputing Center of the University of Oklahoma for allocation of computer times. APPENDIX: THE EXACT THIRD-ORDER BRIDGE TERM B3 BASED ON THE OZ3 EQUATION We give the exact third-order bridge term B3 in terms of h(3) as based on the OZ3 equation (3.4) (using simplified notation for a uniform fluid): 2 − 2ρ d3 C31 γ30 h30 2B3 (10) = ρ 2 d2d3 h20 h30 h123 − γ10 −ρ 3 d4d5d6 C14 γ50 γ60 h456 + ρ3 d3d5d6 C15 γ60 h30 h356 − ρ3 d2d3d5 C15 h20 h30 h235 + ρ 3 d2d4d5 C15 γ40 h20 h245 − ρ d3d6 γ60 h30 h136 + ρ 2 2 d4d6γ40 γ60 h146 2 − ρ 2 d2d4 γ40 h20 h124 + 2ρ d4 C14 γ40 . 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