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Thermodynamic vector units

Let us first compare the thermodynamic vector lengths for these fluids. Because these lengths carry units, we discuss each vector type in turn, comparing different liquids on the common Si-based scale of responsiveness for the specified thermodynamic variable. [Pg.370]

In contrast to the unit dependence of the thermodynamic vector lengths and metric eigenvalues, the thermodynamic angles are pure dimensionless numbers. Figure 11.9 exhibits the angle 6Sy that each entropy vector S) makes with respect to the volume (abscissa) and temperature (ordinate) axes. [Pg.373]

For the case of interest, copolymerization dynamics is described by nonlinear equations (Eq. 62) where variable plays the role of time, supplemented by the thermodynamic relationship (Eq. 63). The instantaneous state of the system characterized by vector X may be represented by a point inside the unit interval X + X2 = 1. The evolution of composition X in the course of... [Pg.178]

The force acting on any differential segment of a surface can be represented as a vector. The orientation of the surface itself can be defined by an outward-normal unit vector, called n. This force vector, indeed any vector, has direction and magnitude, which can be resolved into components in various ways. Normally the components are taken to align with coordinate directions. The force vector itself, of course, is independent of the particular representation. In fluid flow the force on a surface is caused by the compressive (or expansive) and shearing actions of the fluid as it flows. Thermodynamic pressure also acts to exert force on a surface. By definition, stress is a force per unit area. On any surface where a force acts, a stress vector can also be defined. Like the force the stress vector can be represented by components in various ways. [Pg.40]

Here x represents a vector of n continuous variables (e.g., flows, pressures, compositions, temperatures, sizes of units), and y is a vector of integer variables (e.g., alternative solvents or materials) h(x,y) = 0 denote the to equality constraints (e.g., mass, energy balances, equilibrium relationships) g(x,y) < 0 are the p inequality constraints (e.g., specifications on purity of distillation products, environmental regulations, feasibility constraints in heat recovery systems, logical constraints) f(x,y) is the objective function (e.g., annualized total cost, profit, thermodynamic criteria). [Pg.111]

A different approach simulates the thermodynamic parameters of a finite spin system by using Monte Carlo statistics. Both classical spin and quantum spin systems of very large dimension can be simulated, and Monte Carlo many-body simulations are especially suited to fit a spin ensemble with defined interaction energies to match experimental data. In the case of classical spins, the simulations involve solving the equations of motion governing the orientations of the individual unit vectors, coupled to a heat reservoir, that take the form of coupled deterministic nonlinear differential equations.23 Quantum Monte Carlo involves the direct representation of many-body effects in a wavefunction. Note that quantum Monte Carlo simulations are inherently limited in that spin-frustrated systems can only be described at high temperatures.24... [Pg.93]

For thermodynamic vectorial forces, such as a difference in chemical potential of component /, proper spatial characteristics must be assigned for the description of local processes. For this purpose, we consider all points of equal as the potential surface. For the two neighboring equipotential surfaces with chemical potentials p, and /z, + dp the change in p, with number of moles N is dpJdN, which is the measure of the local density of equipotential surfaces. At any point on the potential surface, we construct a perpendicular unit vector with the direction corresponding to the direction of maximal change in p,. With the unit vectors in the direction x, y, and z denoted by i, j, and k, respectively, the gradient of the field in Cartesian coordinates is... [Pg.131]

The idea of overall kinetics could be regarded as just an extreme case of lumping where the projection is onto a one-dimensional subspace, such as the unit vector. In this case the overall lump is just the total mass of the system or of some subset of the compounds. However, overall kinetics (and/or thermodynamics) are in no way exact or approximate lumping procedures, since the lump may well behave in a way that is totally different from that of the original system. [Pg.14]

The E/Z-isomerization process is characterized by angular-dependent excitation and leads, therefore, to the photoselection of a preferred azobezene dye orientation. In other words, the dichroic dye units choose an orientation where the electronic transition moment is perpendicular to the light electric vector. It promotes, in turn, the cooperative reorientation of neighboring moieties, which include other fragments of the macromolecule, such as the main chain or photochemically inactive comonomer units, and low molar mass additives. Thus, a macroscopic orientation of the sample arises, and it remains long after the illumination is stopped and all the dye moieties return to the thermodynamically equilibratory -state. [Pg.146]

In this section, we consider an isothermal, stationary fluid. In this case, from fhermo-dynamics, we know that the only surface force is the normal thermodynamic pressure, p. The pressure at a point P acts normal to any surface through P with a magnitude that is independent of the orientation of the surface. That is, for a surface with orientation denoted by the unit normal vector n, the surface-force vector t(n) takes the form... [Pg.38]

If one looks up the term component in practically any text on physical chemistry or thermodynamics, one finds it is defined as the minimum number of chemical formula units needed to describe the composition of all parts of the system. We say formulas rather than substances because the chemical formulas need not correspond to any actual compounds. For example, a solution of salt in water has two components, NaCl and H2O, even if there is a vapor phase and/or a solid phase (ice or halite), because some combination of those two formulas can describe the composition of every phase. Similarly, a mixture of nitrogen and hydrogen needs only two components, such as N2 and H2, despite the fact that much of the gas may exist as species NH3. Note that although there is always a wide choice of components for a given system (we could equally well choose N and H as our components, or N10 and H10), the number of components for a given system is fixed. The components are simply building blocks , or mathematical entities, with which we are able to describe the bulk composition of any phase in the system. The list of components chosen to represent a system is, in mathematical terms, a basis vector, or simply the basis . [Pg.46]


See other pages where Thermodynamic vector units is mentioned: [Pg.368]    [Pg.368]    [Pg.633]    [Pg.191]    [Pg.185]    [Pg.87]    [Pg.200]    [Pg.54]    [Pg.346]    [Pg.366]    [Pg.370]    [Pg.374]    [Pg.563]    [Pg.304]    [Pg.7]    [Pg.99]    [Pg.106]    [Pg.84]    [Pg.146]    [Pg.346]    [Pg.366]    [Pg.370]    [Pg.374]    [Pg.131]    [Pg.458]    [Pg.623]    [Pg.24]    [Pg.745]    [Pg.780]    [Pg.163]    [Pg.255]    [Pg.223]   
See also in sourсe #XX -- [ Pg.346 , Pg.362 ]

See also in sourсe #XX -- [ Pg.346 , Pg.362 ]




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Thermodynamic vector

Unit vectors

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