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Thermodynamic equation

Thermodynamic equations. For any change of state we have, by the first law, [Pg.149]

As this equation is true for all values of dT and dv, the coefficients of dT and dv must be equal to one another respectively. [Pg.150]

We can eliminate the differential coefficients of the entropy from (5) and (6). Solving (5) for and (6) for and differentiating (5) partially with respect to v and (6) with respect to T, we obtain 32 3 3  [Pg.150]

The expression on the left-hand side of this equation is a measure of the difference of the specific heats — for it follows from the equation, [Pg.150]

An interesting deduction can be made from equation (7) regarding the variation of with the volume. Differentiating (7) with respect to T, we have  [Pg.151]


Clapeyron-Clausius equation A thermodynamic equation applying to any two-phase equilibrium for a pure substance. The equation states ... [Pg.101]

The situation is more complex for rigid media (solids and glasses) and more complex fluids that is, for most materials. These materials have finite yield strengths, support shears and may be anisotropic. As samples, they usually do not relax to hydrostatic equilibrium during an experiment, even when surrounded by a hydrostatic pressure medium. For these materials, P should be replaced by a stress tensor, <3-j, and the appropriate thermodynamic equations are more complex. [Pg.1956]

One can now see why there is not much difference between computed values of Aisotn o and as obtained from the thermodynamic equations in Computer... [Pg.322]

Remember that in this relationship, as in all thermodynamic equations, temperature must be expressed in degrees Kelvin. [Pg.139]

Equation (3.16) shows that the force required to stretch a sample can be broken into two contributions one that measures how the enthalpy of the sample changes with elongation and one which measures the same effect on entropy. The pressure of a system also reflects two parallel contributions, except that the coefficients are associated with volume changes. It will help to pursue the analogy with a gas a bit further. The internal energy of an ideal gas is independent of volume The molecules are noninteracting so it makes no difference how far apart they are. Therefore, for an ideal gas (3U/3V)j = 0 and the thermodynamic equation of state becomes... [Pg.141]

A.queous Solubility. SolubiHty of a chemical in water can be calculated rigorously from equiHbrium thermodynamic equations. Because activity coefficient data are often not available from the Hterature or direct experiments, models such as UNIFAC can be used for stmcture—activity estimations (24). Phase-equiHbrium relationships can then be appHed to predict miscibility. Simplified calculations are possible for low miscibiHty however, when there is a high degree of miscibility, the phase-equiHbrium relationships must be solved rigorously. [Pg.238]

Compiited from the above table with the aid of the thermodynamic equation... [Pg.92]

The expansion coefficient of a solid can be estimated with the aid of an approximate thermodynamic equation of state for solids which equates the thermal expansion coefficient with the quantity where yis the Griineisen dimensionless ratio, C, is the specific heat of the solid, p is the density of the material, and B is the bulk modulus. For fee metals the average value of the Griineisen constant is near 2.3. However, there is a tendency for this constant to increase with atomic number. [Pg.1127]

The jump conditions must be satisfied by a steady compression wave, but cannot be used by themselves to predict the behavior of a specific material under shock loading. For that, another equation is needed to independently relate pressure (more generally, the normal stress) to the density (or strain). This equation is a property of the material itself, and every material has its own unique description. When the material behind the shock wave is a uniform, equilibrium state, the equation that is used is the material s thermodynamic equation of state. A more general expression, which can include time-dependent and nonequilibrium behavior, is called the constitutive equation. [Pg.12]

D.L. Hicks, von Neumann Stability of the Wondy Wavecode for Thermodynamic Equations of State, SAND77-0934, Sandia National Laboratories, Albuquerque, NM, 1977. [Pg.350]

In summaiy, the first law of thermodynamics. Equations la and lb, states that energy is conserved and the energy associated with heat must be included as a form of energy. No process i f is possible if it violates the first law of thermodynamics energy is always conserved in our world as dictated by Equation lb. If Equation lb is applied to an adiabatic process, then because Q = 0 the first part, Equation la is recovered, but one still needs both parts of the first law to define the quantities. [Pg.1127]

Units of Energy 209. The First Law of Thermodynamics 210, Entropy Production Flow Systems 214. Application of (he Second Law 216. Summary of Thermodynamic Equations 223. [Pg.135]

It should be noted that the simple Nernst equation cannot be used since the standard electrode potential is markedly temperature dependent. By means of irreversible thermodynamics equations have been computed to calculate these potentials and are in good agreement with experimentally determined results. [Pg.331]

The Gibbs adsorption equation for the adsorption of an ion / from solution can be written in the form of the thermodynamic equation... [Pg.1176]

Otherwise it has been shown that the accumulation of electrolytes by many cells runs at the expense of cellular energy and is in no sense an equilibrium condition 113) and that the use of equilibrium thermodynamic equations (e.g., the Nemst-equation) is not allowed in systems with appreciable leaks which indicate a kinetic steady-state 114). In addition, a superposition of partial current-voltage curves was used to explain the excitability of biological membranes112 . In interdisciplinary research the adaptation of a successful theory developed in a neighboring discipline may be beneficial, thus an attempt will be made here, to use the mixed potential model for ion-selective membranes also in the context of biomembrane surfaces. [Pg.237]

In the late eighteenth century Priestley prepared ammonia by reacting HN03(g) with hydrogen gas. The thermodynamic equation for the reaction is... [Pg.221]

In 1879 Lord Kelvin introduced the term nwtivity for the possession, the waste of which is called dissipation at constant temperature this is identical with Maxwell s available energy. He showed in a paper On Thermodynamics founded on Motivity and Energy Phil. Mag., 1898), that all the thermodynamic equations could be derived from the properties of motivity which follow directly from Carnot s theorem, without any explicit introduction of the entropy. [Pg.101]

In the applications of the thermodynamic equations of equilibrium to gaseous systems we shall take in ... [Pg.328]

Students often ask, What is enthalpy The answer is simple. Enthalpy is a mathematical function defined in terms of fundamental thermodynamic properties as H = U+pV. This combination occurs frequently in thermodynamic equations and it is convenient to write it as a single symbol. We will show later that it does have the useful property that in a constant pressure process in which only pressure-volume work is involved, the change in enthalpy AH is equal to the heat q that flows in or out of a system during a thermodynamic process. This equality is convenient since it provides a way to calculate q. Heat flow is not a state function and is often not easy to calculate. In the next chapter, we will make calculations that demonstrate this path dependence. On the other hand, since H is a function of extensive state variables it must also be an extensive state variable, and dH = 0. As a result, AH is the same regardless of the path or series of steps followed in getting from the initial to final state and... [Pg.20]

Derivation of Thermodynamic Equations Using the Properties of the Exact Differential... [Pg.28]

We have seen how to calculate q for the isochoric and isobaric processes. We indicated in Chapter 1 that q = 0 for an adiabatic process (by definition). For an isothermal process, the calculation of q requires the application of other thermodynamic equations. For example, q can be obtained from equation (2.3) if AC and w can be calculated. The result is... [Pg.56]

Thus, in a reversible process that is both isothermal and isobaric, dG equals the work other than pressure-volume work that occurs in the process." Equation (3.96) is important in chemistry, since chemical processes such as chemical reactions or phase changes, occur at constant temperature and constant pressure. Equation (3.96) enables one to calculate work, other than pressure-volume work, for these processes. Conversely, it provides a method for incorporating the variables used to calculate these forms of work into the thermodynamic equations. [Pg.147]

First, we note that all of the thermodynamic equations that we have derived for the total extensive variables apply to the partial molar properties. Thus, if... [Pg.210]


See other pages where Thermodynamic equation is mentioned: [Pg.3]    [Pg.351]    [Pg.317]    [Pg.49]    [Pg.141]    [Pg.507]    [Pg.506]    [Pg.349]    [Pg.1504]    [Pg.242]    [Pg.16]    [Pg.364]    [Pg.50]    [Pg.902]    [Pg.200]    [Pg.365]    [Pg.223]    [Pg.103]    [Pg.105]    [Pg.107]    [Pg.109]    [Pg.111]    [Pg.113]    [Pg.115]    [Pg.329]    [Pg.82]    [Pg.106]    [Pg.117]   
See also in sourсe #XX -- [ Pg.161 , Pg.162 , Pg.163 , Pg.164 , Pg.165 , Pg.166 , Pg.167 , Pg.168 , Pg.169 , Pg.170 , Pg.171 , Pg.172 , Pg.173 , Pg.174 , Pg.175 , Pg.176 , Pg.177 , Pg.178 ]

See also in sourсe #XX -- [ Pg.169 ]




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