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Energy constant-volume

Eq. (1) would correspond to a constant energy, constant volume, or micro-canonical simulation scheme. There are various approaches to extend this to a canonical (constant temperature), or other thermodynamic ensembles. (A discussion of these approaches is beyond the scope of the present review.) However, in order to perform such a simulation there are several difficulties to overcome. First, the interactions have to be determined properly, which means that one needs a potential function which describes the system correctly. Second, one needs good initial conditions for the velocities and the positions of the individual particles since, as shown in Sec. II, simulations on this detailed level can only cover a fairly short period of time. Moreover, the overall conformation of the system should be in equilibrium. [Pg.485]

These equations of motion can be integrated by many standard ensembles constant energy, constant volume, constant temperature and constant pressure. More complex forms of the extended Lagrangian are possible and readers are referred to Ref. [17] for a Lagrangian that allows intermolecular charge transfer. [Pg.242]

A = Helmholtz free energy (constant volume and temperature) dW = the elastic work... [Pg.392]

In an isolated system (constant energy, constant volume, and constant number of moles), the equilibrium state is the state that maximizes entropy ... [Pg.167]

Helmholtz free energy The maximum amount of energy available to do work resulting from changes in a system at constant volume. See free energy and Gibbs-Helmholtz equation. [Pg.201]

If the process is carried out at constant volume, the heat evolved Qi will be equal to an energy change AE2 or, per mole of adsorbate, qi = Ae2 (small capital letters will be used to denote mean molar quantities). Alternatively, the process may be... [Pg.642]

The heat evolved will now be a differential heat of adsorption, equal at constant volume to Qd or per mole, to qd - AI2, where Ae2 is the change in partial molar energy. It follows that... [Pg.642]

Note that in this special case, the heat absorbed directly measures a state fiinction. One still has to consider how this constant-volume heat is measured, perhaps by an electric heater , but then is this not really work Conventionally, however, if work is restricted to pressure-volume work, any remaining contribution to the energy transfers can be called heat . [Pg.345]

Thus for isobaric processes a new fimction, the enthalpy H, has been introduced and its change A// is more directly related to the heat that must have been absorbed than is the energy change At/. The same reservations about the meanmg of heat absorbed apply in this process as in the constant-volume process. [Pg.346]

In many experiments the sample is in thennodynamic equilibrium, held at constant temperature and pressure, and various properties are measured. For such experiments, the T-P ensemble is the appropriate description. In this case the system has fixed and shares energy and volume with the reservoir E = E + E" and V=V + V", i.e. the system... [Pg.417]

Fluctuations of observables from their average values, unless the observables are constants of motion, are especially important, since they are related to the response fiinctions of the system. For example, the constant volume specific heat of a fluid is a response function related to the fluctuations in the energy of a system at constant N, V and T, where A is the number of particles in a volume V at temperature T. Similarly, fluctuations in the number density (p = N/V) of an open system at constant p, V and T, where p is the chemical potential, are related to the isothemial compressibility iCp which is another response fiinction. Temperature-dependent fluctuations characterize the dynamic equilibrium of themiodynamic systems, in contrast to the equilibrium of purely mechanical bodies in which fluctuations are absent. [Pg.437]

The molar Helmholtz free energy of mixing (appropriate at constant volume) for such a synnnetrical system of molecules of equal size, usually called a simple mixture , is written as a fiinction of the mole fraction v of the component B... [Pg.627]

The first law of thennodynamics relates the energy change m a system at constant volume to the work done on the system and the heat added to the system q. [Pg.1899]

Values of COT) can be derived from a constant volume calorimeter by measuring AU for small values of Tj - TO and evaluating AU/(T2 - T ) as a fiinction of temperature. The energy change AU can be derived from a knowledge of tlie amount of electrical energy required to change the temperature of the sample + container... [Pg.1900]

Just as one may wish to specify the temperature in a molecular dynamics simulation, so may be desired to maintain the system at a constant pressure. This enables the behavior of the system to be explored as a function of the pressure, enabling one to study phenomer such as the onset of pressure-induced phase transitions. Many experimental measuremen are made under conditions of constant temperature and pressure, and so simulations in tl isothermal-isobaric ensemble are most directly relevant to experimental data. Certai structural rearrangements may be achieved more easily in an isobaric simulation than i a simulation at constant volume. Constant pressure conditions may also be importai when the number of particles in the system changes (as in some of the test particle methoc for calculating free energies and chemical potentials see Section 8.9). [Pg.401]

Since the solvent molecules, the polymer segments, and the lattice sites are all assumed to be equal in volume, reaction (8.A) impUes constant volume conditions. Under these conditions, AU is needed and what we have called Aw might be better viewed as the contribution to the internal energy of a pairwise interaction AUp jj., where the subscript reminds us that this is the contribution of a single pair formation by reaction A. [Pg.523]

The integrated terms are simply the specific heat of the unit mass of adsorbent and its associated adsorbate. The specific heat at constant volume has been used for the adsorbate since, theoretically, there is no expansion of the adsorbate volume and the heat required to raise the temperature is the change in internal energy. In practice there will be some expansion and a pessimistically high estimate could use the specific heat at constant pressure The specific heat of the adsorbed phase is in any case difficult to estimate and it is common to approximate it to that of saturated liquid adsorbate at the same temperature. [Pg.314]

The gas phase decomposition A B -r 2C is conducted in a constant volume reactor. Runs 1 through 5 were conducted at 100°C run 6 was performed at 110°C (Table 3-15). Determine (1) the reaction order and the rate constant, and (2) the activation energy and frequency factor for this reaction. [Pg.195]

These relationships enable the combination of the mass and the energy balances. For constant volume and density, with m = pV, ... [Pg.459]

Suppose now that we have an ensemble of N non-interacting particles in a thermally insulated enclosure of constant volume. This statement means that the number of particles, the internal energy and the volume are constant and so we are dealing with a microcanonical ensemble. Suppose that each of the particles has quantum states with energies given by i, 2,... and that, at equilibrium there are Ni particles in quantum state Su particles in quantum state 2, and so on. [Pg.60]

The heat capacity at constant volume is the derivative of the energy with respect to temperature at constant volume (eq. (16.1). There are several ways of calculating such response properties. The most accurate is to perform a series of simulations under NVT conditions, and thereby determine the behaviour of (f/) as a function of T (for example by fitting to a suitable function). Subsequently this function may be differentiated to give the heat capacity. This approach has the disadvantage that several simulations at different temperatures are required. Alternatively, the heat capacity can be calculated from the fluctuation of the energy around its mean value. [Pg.378]

Fig. 3 Total energy of CuZn for different c/a ratios and constant volume (a). Binding energy versus volume curves (b) for fct (circle) and B2 (square) unit cell. Fig. 3 Total energy of CuZn for different c/a ratios and constant volume (a). Binding energy versus volume curves (b) for fct (circle) and B2 (square) unit cell.
A = work function (Helmholtz free energy), Btu/lb or Btu C = heat capacity, Btu/lb °R Cp = heat capacity at constant pressure = heat capacity at constant volume F= (Gibbs) free energy, Btu/lb or Btu g = acceleration due to gravity = 32.174 ft/s ... [Pg.209]

Some mechanically driven systems include heated vessels or spraying of the water to enhance the natural evaporation rate. In heating, the energy needed to evaporate the water is equal to that needed to bring the water to the temperature of vaporization plus that energy required for the evaporation, where for constant volume this is... [Pg.1357]


See other pages where Energy constant-volume is mentioned: [Pg.46]    [Pg.6]    [Pg.46]    [Pg.6]    [Pg.190]    [Pg.393]    [Pg.411]    [Pg.442]    [Pg.621]    [Pg.622]    [Pg.687]    [Pg.1910]    [Pg.641]    [Pg.642]    [Pg.62]    [Pg.99]    [Pg.317]    [Pg.351]    [Pg.502]    [Pg.506]    [Pg.1338]    [Pg.111]    [Pg.99]    [Pg.456]    [Pg.252]    [Pg.58]    [Pg.83]    [Pg.1035]    [Pg.530]   


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