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Quantity thermodynamic

The First Law of Thermodynamics Any Change in the Energy of a System Requires an Equal and Opposite Change in the Surroundings The Second Law of Thermodynamics In Any Spontaneous Process the Total Entropy of the System and the Surroundings Increases Free Energy Provides the Most Useful Criterion for Spontaneity [Pg.30]

Values of Free Energy Are Known for Many Compounds [Pg.30]

The Standard Free Energy Change in a Reaction Is Related Logarithmically to the Equilibrium Constant [Pg.30]

Free Energy Is the Maximum Energy Available for Useful Work [Pg.30]

Biological Systems Perform Various Kinds of Work Favorable Reactions Can Drive Unfavorable Reactions [Pg.30]

There are several different energetic quantities that are relevant to quantum chemical evaluation of H-bond strength. The interaction of a pair of molecules, A and B, with one another to form an A-- B complex can be represented by the reaction [Pg.15]

For most complexation reactions, the complex is more stable than the isolated species so the process is exothermic and AE is negative. All species are normally taken in their fully optimized geometries. It is important to note that the process of combining with one another [Pg.15]

A typical calculation of a molecular interaction thus involves the geometry optimization of three entities the reactants A and B, and the complex A---B. The subtraction of electronic energies in Equation (1.4) yields the electronic contribution to the interaction en- [Pg.16]

The rotational partition function is dependent upon the equilibrium geometry. Assuming separation of rotational and vibrational motions. [Pg.16]

A given molecule has 3n-6 normal modes of vibration (3n-5 if linear), where n is the number of atoms. Each mode i has a characteristic vibrational frequency Vj and a residual energy even at absolute zero temperature. The total zero-point vibrational energy is thus  [Pg.16]

The composition of a solution is obviously one of its important properties. In the preceding section various ways of describing the composition of a two-component system were described. Other properties include its volume, V, internal energy, U, and entropy, S. In order to specify any one of these, one must specify not only the amounts of each of the components but also the temperature, T, and pressure, P. These quantities are known as the independent variables of the system. They are [Pg.6]

Consider first of all the volume of the solution. The volume of any solution may be estimated from the mass of each component and its density. Volume is an extensive property, since its value depends on the total amount of solution. A quantity of more fundamental interest is the specific volume, Cg, that is, the volume per gram. It is simply the reciprocal of the density. This is an intensive quantity, since its value does not depend on the size of the solution, only on its composition, temperature, and pressure. From the point of view of chemists, an even better way to describe this property is in terms of the molar volume, that is, the volume per mole of solution. For a two-component solution, the molar volume Fjj, is related to the density as follows  [Pg.7]

Notice that the units of this quantity are L mol if the density is expressed in g L. To calculate the volume from the molar volume one must know the number of moles of each component, d j. Thus, [Pg.7]

It was pointed out above that the volume is a function of the number of moles of each component, temperature, and pressure. Thus, one may write for a two-component system [Pg.7]

It follows that the total derivative of the volume dV is given by [Pg.7]

It is a matter of interest to assess how of a homopolymer depends on the chemical nature and structure of its chain repeating unit. The melting temperature is uniquely described by the ratio of the heat of fusion to entropy of fusion, per repeating unit. Therefore, attention should be focused on how these two independent quantities depend on structure. The enthalpies of fusion per chain repeating unit are experimentally accessible for many polymers. From these data, and T, it is possible to develop an understanding of the molecular and structural basis of the thermodynamic quantities that govern fusion. [Pg.236]

As energy is conserved, the change of the internal energy t/ of a system equals the heat dQ absorbed and the mechanical work dW done to the system, dU =dQ + dW. When the volume of the system changes by dV under the pressure P, the mechanical work done to the system is given by [Pg.7]

When there is no mechanical work, the heat absorbed equals the change of internal energy. From the definition of ternperamre l/T= (jp)y, the heat absorbed in a reversible process at constant volume is [Pg.7]

The internal energy U, entropy S, and volume V are extensive quantities, while temperature T and pressure P are intensive quantities. The enthalpy H of the system is defined by [Pg.8]

From this equation, it can be seen that the physical meaning of enthalpy is that in a process at constant pressure (dP = 0), the change of enthalpy dH is equal to the heat absorbed dQ =TdS)). The derivatives of the enthalpy are [Pg.8]


Thermodynamic quantities which refer to the standard state are denoted by superscript zeros ( ), e.g. AG/, AH/, AS/, the subscript denoting the temperature T of the system. [Pg.370]

The relations which permit us to express equilibria utilize the Gibbs free energy, to which we will give the symbol G and which will be called simply free energy for the rest of this chapter. This thermodynamic quantity is expressed as a function of enthalpy and entropy. This is not to be confused with the Helmholtz free energy which we will note sF (L" j (j, > )... [Pg.148]

TTie calculation of partial fugacltles requires knowing the derivatives of thermodynamic quantities with respect to the compositions and to arrive at a mathematical model reflecting physical reality. [Pg.152]

Systems involving an interface are often metastable, that is, essentially in equilibrium in some aspects although in principle evolving slowly to a final state of global equilibrium. The solid-vapor interface is a good example of this. We can have adsorption equilibrium and calculate various thermodynamic quantities for the adsorption process yet the particles of a solid are unstable toward a drift to the final equilibrium condition of a single, perfect crystal. Much of Chapters IX and XVII are thus thermodynamic in content. [Pg.2]

A number of methods have been described in earlier sections whereby the surface free energy or total energy could be estimated. Generally, it was necessary to assume that the surface area was known by some other means conversely, if some estimate of the specific thermodynamic quantity is available, the application may be reversed to give a surface area determination. This is true if the heat of solution of a powder (Section VII-5B), its heat of immersion (Section X-3A), or its solubility increase (Section X-2) are known. [Pg.576]

There are alternative ways of defining the various thermodynamic quantities. One may, for example, treat the adsorbed film as a phase having volume, so that P, V terms enter into the definitions. A systematic treatment of this type has been given by Honig [116], who also points out some additional types of heat of adsorption. [Pg.646]

Rickman J M and Phillpot S R 1991 Temperature dependence of thermodynamic quantities from simulations at a single temperature Phys. Rev.L 66 349-52... [Pg.2280]

Conformational free energy simulations are being widely used in modeling of complex molecular systems [1]. Recent examples of applications include study of torsions in n-butane [2] and peptide sidechains [3, 4], as well as aggregation of methane [5] and a helix bundle protein in water [6]. Calculating free energy differences between molecular states is valuable because they are observable thermodynamic quantities, related to equilibrium constants and... [Pg.163]

Once the phonon frequencies are known it becomes possible to determine various thermodynamic quantities using statistical mechanics (see Appendix 6.1). Here again some slight modifications are required to the standard formulae. These modifications are usually a consequence of the need to sum over the points sampled in the Brillouin zone. For example, the zero-point energy is ... [Pg.313]

Ire boundary element method of Kashin is similar in spirit to the polarisable continuum model, lut the surface of the cavity is taken to be the molecular surface of the solute [Kashin and lamboodiri 1987 Kashin 1990]. This cavity surface is divided into small boimdary elements, he solute is modelled as a set of atoms with point polarisabilities. The electric field induces 1 dipole proportional to its polarisability. The electric field at an atom has contributions from lipoles on other atoms in the molecule, from polarisation charges on the boundary, and where appropriate) from the charges of electrolytes in the solution. The charge density is issumed to be constant within each boundary element but is not reduced to a single )oint as in the PCM model. A set of linear equations can be set up to describe the electrostatic nteractions within the system. The solutions to these equations give the boundary element harge distribution and the induced dipoles, from which thermodynamic quantities can be letermined. [Pg.614]

Molecular descriptors must then be computed. Any numerical value that describes the molecule could be used. Many descriptors are obtained from molecular mechanics or semiempirical calculations. Energies, population analysis, and vibrational frequency analysis with its associated thermodynamic quantities are often obtained this way. Ah initio results can be used reliably, but are often avoided due to the large amount of computation necessary. The largest percentage of descriptors are easily determined values, such as molecular weights, topological indexes, moments of inertia, and so on. Table 30.1 lists some of the descriptors that have been found to be useful in previous studies. These are discussed in more detail in the review articles listed in the bibliography. [Pg.244]

These equations, relating to oi,s, and E t,g to Egy, show that 3od can be calculated for a reaction proceeding through the equilibrium concentration of a free base if the thermodynamic quantities relating to the ionisation of the base, and the appropriate acidity function and its temperature coefficient are known (or alternatively, if the ionisation ratio and its temperature coefficient are known under the appropriate conditions for the base. )... [Pg.158]

The values of fH° and Ay.G° that are given in the tables represent the change in the appropriate thermodynamic quantity when one mole of the substance in its standard state is formed, isothermally at the indicated temperature, from the elements, each in its appropriate standard reference state. The standard reference state at 25°C for each element has been chosen to be the standard state that is thermodynamically stable at 25°C and 1 atm pressure. The standard reference states are indicated in the tables by the fact that the values of fH° and Ay.G° are exactly zero. [Pg.532]

Next we consider how to evaluate the factor 6p. We recognize that there is a local variation in the Gibbs free energy associated with a fluctuation in density, and examine how this value of G can be related to the value at equilibrium, Gq. We shall use the subscript 0 to indicate the equilibrium value of free energy and other thermodynamic quantities. For small deviations from the equilibrium value, G can be expanded about Gq in terms of a Taylor series ... [Pg.681]

The terms AG, AH, and AS are state functions and depend only on the identity of the materials and the initial and final state of the reaction. Tables of thermodynamic quantities are available for most known materials (see also Thermodynamic properties) (11,12). [Pg.506]

We will be looking at kinetics in Chapter 6. But before we can do this we need to know what we mean by driving forces and how we calculate them. In this chapter we show that driving forces can be expressed in terms of simple thermodynamic quantities, and we illustrate this by calculating driving forces for some typical processes like solidification, changes in crystal structure, and precipitate coarsening. [Pg.46]

Many thermodynamic quantities can be calculated from the set of normal mode frequencies. In calculating these quantities, one must always be aware that the harmonic approximation may not provide an adequate physical model of a biological molecule under physiological conditions. [Pg.156]

Temperature becomes a quantity definable either in terms of macroscopic thermodynamic quantities, such as heat and work, or, with equal validity and identical results, in terms of a quantity, which characterized the energy distribution among the particles in a system. With this understanding of the concept of temperature, it is possible to explain how heat (thermal energy) flows from one body to another. [Pg.3]

A MC study of adsorption of living polymers [28] at hard walls has been carried out in a grand canonical ensemble for semiflexible o- 0 polymer chains and adsorbing interaction e < 0 at the walls of a box of size C. A number of thermodynamic quantities, such as internal energy (per lattice site) U, bulk density (f), surface coverage (the fraction of the wall that is directly covered with segments) 9, specific heat C = C /[k T ]) U ) — U) ), bulk isothermal compressibility... [Pg.532]

Nevertheless, large-scale phenomena and complicated phase diagrams cannot be investigated within realistic models at the moment, and this is not very likely to change soon. Therefore, theorists have often resorted to coarse-grained models, which capture the features of the substances believed to be essential for the properties of interest. Such models can provide qualitative and semiquantitative insight into the physics of these materials, and hopefully establish general relationships between microscopic and thermodynamic quantities. [Pg.637]

The thermodynamic quantities and correlation functions can be obtained from Eq. (1) by functional integration. However, the functional integration cannot usually be performed exactly. One has to use approximate methods to evaluate the functional integral. The one most often used is the mean-field approximation, in which the integral is replaced with the maximum of the integrand, i.e., one has to find the minimum of. F[(/)(r)], which satisfies the mean-field equation... [Pg.692]

According to this very simple derivation and result, the position of the transition state along the reaction coordinate is determined solely by AG° (a thermodynamic quantity) and AG (a kinetic quantity). Of course, the potential energy profile of Fig. 5-15, upon which Eq. (5-60) is based, is very unrealistic, but, quite remarkably, it is found that the precise nature of the profile is not important to the result provided certain criteria are met, and Miller " obtained Eq. (5-60) using an arc length minimization criterion. Murdoch has analyzed Eq. (5-60) in detail. Equation (5-60) can be considered a quantitative formulation of the Hammond postulate. The transition state in Fig. 5-9 was located with the aid of Eq. (5-60). [Pg.224]

These same dependencies will, in general, apply to the heat of ionization of the buffer acid, AH. Thermodynamic quantities, namely, AH°, have been reported for some buffer substances, and it is found that A//° is temperature dependent. Bates and Hetzer studied the temperature dependence of for the important buffer tris(hydroxymethyl)aminomethane (TRIS), finding... [Pg.258]

These authors also list thermodynamic quantities for many other amines. A// , at 25°C, ranges from 3.37 kcal mol for the very weakly basic 2,2 -bipyridinium to 13.88 kcal mol for -butylammonium for TRIS at 25°C, A// = 11.38 kcal mol . ... [Pg.258]

It may happen that AH is not available for the buffer substance used in the kinetic studies moreover the thermodynamic quantity A//° is not precisely the correct quantity to use in Eq. (6-37) because it does not apply to the experimental solvent composition. Then the experimentalist can determine AH. The most direct method is to measure AH calorimetrically however, few laboratories Eire equipped for this measurement. An alternative approach is to measure K, under the kinetic conditions of temperature and solvent this can be done potentiometrically or by potentiometry combined with spectrophotometry. Then, from the slope of the plot of log K a against l/T, AH is calculated. Although this value is not thermodynamically defined (since it is based on the assumption that AH is temperature independent), it will be valid for the present purpose over the temperature range studied. [Pg.258]


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Absolute thermodynamic quantities

Adsorption thermodynamic quantities

Compound thermodynamic quantities

Determination of thermodynamic quantities

ESTIMATION OF THERMODYNAMIC QUANTITIES

Evidence from Thermodynamic Quantities

Excess Nature of Interfacial Thermodynamic Quantities The Gibbs Dividing Plane

Excess thermodynamic quantities

Experimental techniques for determining thermodynamic quantities of biopolymer interactions in solution

Extensive thermodynamic quantities

Extracting the thermodynamic quantities of solvation from experimental data

Fluid system thermodynamic quantities

Flux, of thermodynamic quantity

INNATE THERMODYNAMIC QUANTITIES

Intensive thermodynamic quantities

Ionic thermodynamic quantities

Kirkwood-Buff theory thermodynamic quantities

Light Scattering thermodynamic quantities

Liquids, thermodynamic quantities

Measurable quantities in thermodynamics

Measurement of Thermodynamic Quantities

Molecular system thermodynamical quantities

Other thermodynamic quantities of solvation

Partial molal quantities thermodynamics

Partial molal quantities—review of thermodynamics

Physical and thermodynamic quantities at the interface

Poly diluent equation thermodynamic quantities

Poly indirect method thermodynamic quantities

Potential energy surface thermodynamic quantities

Properties thermodynamic quantities

Proteins thermodynamic quantities

Quantities, thermodynamic, calculating

Reaction thermodynamic — quantity

Relation of emfs to thermodynamic quantities

Relations between Thermodynamic Quantities and GMDFs

Relations between thermodynamic quantities and generalized molecular distribution functions

Solids, thermodynamic quantities

Standard Thermodynamic Quantities of a Chemical Reaction

Standard thermodynamic quantities

Standard thermodynamic quantities of transfer

Statistical Mechanical Expressions for the Solvation Thermodynamic Quantities

Surface Thermodynamic Quantities for a Pure Substance

The temperature coefficient in relation to thermodynamic quantities

Thermodynamic Quantities Governing Melting

Thermodynamic Quantities Pertaining to Ion Association

Thermodynamic Quantities for Pure Liquids and Solids

Thermodynamic Quantities for the

Thermodynamic Quantities for the Ionization Reactions of Buffers

Thermodynamic Quantities for the Ionization Reactions of Buffers in Water

Thermodynamic Quantities for the in Water

Thermodynamic Quantities in Reversible Expansions

Thermodynamic Quantities of Solvation from Experimental Data

Thermodynamic functions/quantitie

Thermodynamic quantities calculation

Thermodynamic quantities entropy

Thermodynamic quantities expressed in terms of molecular distribution functions

Thermodynamic quantities in electrochemistry effect of temperature on emf

Thermodynamic quantities in electrochemistry relation of AG to

Thermodynamic quantities, apparent

Thermodynamic quantities, benzene

Thermodynamic quantities, estimation

Thermodynamic quantities, reduced

Thermodynamics calculating quantities

Thermodynamics indicating quantities

Thermodynamics molar quantities

Thermodynamics quantities fluid system

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