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Homogeneous reference fluid

Minimization of the functional in Eq. (57) gives the local structure in the homogeneous reference fluid approximation (HRFA) (Ramirez and Borgis, 2005)... [Pg.38]

In general, any substance that is above the temperature and pressure of its thermodynamic critical point is called a supercritical fluid. A critical point represents a limit of both equilibrium and stability conditions, and is formally delincd as a point where the first, second, and third derivatives of the energy basis function for a system equal zero (or, more precisely, where 9P/9V r = d P/dV T = 0 for a pure compound). In practical terms, a critical point is identifled as a point where two or more coexisting fluid phases become indistinguishable. For a pure compound, the critical point occurs at the limit of vapor-Uquid equilibrium where the densities of the two phases approach each other (Figures la and lb). Above this critical point, no phase transformation is possible and the substance is considered neither a Uquid nor a gas, but a homogeneous, supercritical fluid. The particular conditions (such as pressure and temperature) at which the critical point of a substance is achieved are unique for every substance and are referred to as its critical constants (Table 1). [Pg.386]

It should be intuitively clear that the correlation between any two particles vanishes as ri — r21 oo. Therefore g -> 1 and /i 0 in this limit. For homogeneous fluids all positions are equivalent, and it follows that g(ri, r2) = gCfi — i 2)- For homogeneous-isotropic fluids g(ri, r2) = g( ri — r2 ), and similarly for h. In this case we refer to these functions as radial distribution functions. [Pg.181]

Consider a reference plane (a Une in two dimensions) normal in the y-direction embedded in a homogeneous fluid in equilibrium. The fluid below the plane exerts a mean force per unit area on the fluid above the plane by Newton s third law, the fluid above the plane must exert a mean force -py on the fluid below the plane. The normal force per unit area is just the mean pressure, P, so that pyy = P. In a homogeneous simple fluid in which there are no velocity gradients, there is no tangential force, so that, for example, pyx = 0. p p is called the pressure tensor, and the last result is just a statement of the well-known fact that the pressure tensor in a homogeneous simple fluid at equilibrium has no off-diagonal elements the diagonal elements are all equal to the mean pressure P. [Pg.13]

Not all elements of the industrial thermocouple need to be wine. For example, if a copper pipe contains a flowing fluid whose temperature is to be measured, a constantan wine attached to the pipe will form a T, or copper—constantan, thermocouple. Such arrangements ate difficult to caUbrate and requite full understanding of the possible inherent problems. For example, is the copper pipe fully annealed Homogeneous Pure, or an alloy Many ingenious solutions to specific measurement problems ate given in Reference 6. [Pg.403]

Fluidization may be described as incipient buoyancy because the particles are still so close as to have essentially no mobility, whereas the usual desire in fluidization is to create bed homogeneity. Such homogeneity can be achieved only by violent mixing. This is brought about by increasing the fluid velocity to the point of blowing "bubbles" or voids into the bed, which mix the bed as they rise. The increased fluid velocity at which bubbles form first is referred to as the incipient (or minimum) bubbling velocity. [Pg.478]

The ideal tubular reactor is one in which elements of the homogeneous fluid reactant move through a tube as plugs moving parallel to the tube axis. This flow pattern is referred to as... [Pg.247]

In principle, the energy dissipation (friction loss) associated with the gas-liquid, gas-wall, and liquid-wall interactions can be evaluated and summed separately. However, even for distributed (nonhomogeneous) flows it is common practice to evaluate the friction loss as a single term, which, however, depends in a complex manner on the nature of the flow and fluid properties in both phases. This is referred to as the homogeneous model ... [Pg.462]

Furthermore, the closures for the fluid—particle drag and the particle-phase stresses that we discussed were all derived from data or analysis of nearly homogeneous systems. In what follows, we refer to the TFM equations with closures deduced from nearly homogeneous systems as the microscopic TFM equations. The kinetic theory based model equations fall in this category. [Pg.133]

J. F. Brennecke, J. E Chateauneuf, Homogeneous Organic Reactions as Mechanistic Probes in Supercritical Fluids , Chem. Rev. 1999, 99, 433-452, and references cited therein. [Pg.25]

Human serum is relatively more characterised than other biological samples and as a result some information on various metal binding proteins exists in various reference books. However, in samples for which such information is not available most investigators have resorted to calibrating the column with proteins or molecules of known molecular masses. Sample types to which this approach has been applied include serum, milk, amniotic fluid, urine and tissue homogenates. Some of the applications of SEC are summarised in Table 1. [Pg.157]

Fluid-bed catalysts. The use of fluid-bed catalysts represents an attempt to homogenize heterogeneous catalysts. We shall not pursue this area here the interested reader is referred to Flood and Lee (32) for an introductory article to this field. [Pg.192]


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Homogeneous reference fluid approximation

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