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Equations of state using

The fugacity coefficient can be found from the equation of state using the thermodynamic relation (Beattie, 1949) ... [Pg.26]

Berthelot s equation of state, used by many thermodynamicists, is... [Pg.529]

The density of Hquid carbon monoxide at various temperatures is Hsted in Table 4 (5,7). The density of gaseous carbon monoxide (7) can be calculated direcdy from the equation of state using the compressibihty factor at the temperature and pressure of interest. [Pg.49]

Several colloidal systems, that are of practical importance, contain spherically symmetric particles the size of which changes continuously. Polydisperse fluid mixtures can be described by a continuous probability density of one or more particle attributes, such as particle size. Thus, they may be viewed as containing an infinite number of components. It has been several decades since the introduction of polydispersity as a model for molecular mixtures [73], but only recently has it received widespread attention [74-82]. Initially, work was concentrated on nearly monodisperse mixtures and the polydispersity was accounted for by the construction of perturbation expansions with a pure, monodispersive, component as the reference fluid [77,80]. Subsequently, Kofke and Glandt [79] have obtained the equation of state using a theory based on the distinction of particular species in a polydispersive mixture, not by their intermolecular potentials but by a specific form of the distribution of their chemical potentials. Quite recently, Lado [81,82] has generalized the usual OZ equation to the case of a polydispersive mixture. Recently, the latter theory has been also extended to the case of polydisperse quenched-annealed mixtures [83,84]. As this approach has not been reviewed previously, we shall consider it in some detail. [Pg.154]

It is obvious that the calculated TCJ depends strongly on the equation of state used in the computation. Unfortunately, as already stated, there are no unequivocal exptl T j s for PETN (and probably not for any expl) to compare theory and expt. However, note that for all three equations of state cited above, T j increases as pD decreases... [Pg.575]

Englezos, P., G. Bygrave, and N. Kalogerakis, "Interaction Parameter Estimation in Cubic Equations of State Using Binary Phase Equilibrium Critical Point Data", Ind. Eng Chem. Res.31(5), 1613-1618 (1998). [Pg.394]

Englezos, P., N. Kalogerakis and P.R. Bishnoi, "A Systematic Approach for the Efficient Estimation of Interaction Parameters in Equations of State Using Binary VLE Data", Can. J. Chem. Eng., 71,322-326 (1993). [Pg.394]

This calculation assumed the gas to be ideal. For comparison, the calculation can be based on the Peng-Robinson Equation of State (see Chapter 4). A number of commercial physical property software packages allow the prediction of gas density and y for a mixture of hydrogen and methane using the Peng-Robinson Equation of State. Using this, the gas density at normal conditions is 0.1651 kg-rn 3. At 40°C and 81 bar, the density is 11.2101 kg-rn 3. Thus, suction volume of gas... [Pg.275]

The major difficulty in applying this hydrodynamic theory of detonation to practical cases lies in the calculation of E2, the specific internal energy of the explosion products immediately behind the detonation front, without which the Rankine-Hugoniot curve cannot be drawn. The calculations require a knowledge of the equation of state of the detonation products and also a full knowledge of the chemical equilibria involved, both at very high temperatures and pressures. The first equation of state used was the Abel equation... [Pg.19]

Tables 2.1 and 2.2 show that theory enables detonation velocities to be calculated in close agreement with those observed experimentally. This, unfortunately, is not a critical test of the theory as velocities when calculated are rather insensitive to the nature of the equation of state used. A better test would be to calculate the peak pressures, densities and temperatures encountered in detonation, and compare these with experimental results. The major difficulties here are experimental. Attempts to measure temperatures in the detonation zone have not been very successful, but better results have been obtained in the measurement of densities and pressures. Schall introduced density measurement by very short X-ray flash radiography and showed that TNT at an initial density of 1 -50 increased 22% in density in the detonation wave. More recently detonation pressures have been measured by Duff and Houston using a method (introduced by Goranson) in which the pressure is deduced from the velocity imparted to a metal plate placed at the end of the column of explosive. Using this method, for example, Deal obtains the detonation pressures for some military explosives recorded in Table 2.3. More... Tables 2.1 and 2.2 show that theory enables detonation velocities to be calculated in close agreement with those observed experimentally. This, unfortunately, is not a critical test of the theory as velocities when calculated are rather insensitive to the nature of the equation of state used. A better test would be to calculate the peak pressures, densities and temperatures encountered in detonation, and compare these with experimental results. The major difficulties here are experimental. Attempts to measure temperatures in the detonation zone have not been very successful, but better results have been obtained in the measurement of densities and pressures. Schall introduced density measurement by very short X-ray flash radiography and showed that TNT at an initial density of 1 -50 increased 22% in density in the detonation wave. More recently detonation pressures have been measured by Duff and Houston using a method (introduced by Goranson) in which the pressure is deduced from the velocity imparted to a metal plate placed at the end of the column of explosive. Using this method, for example, Deal obtains the detonation pressures for some military explosives recorded in Table 2.3. More...
Evaluation of Various Theoretical Equations of State used in Calculation of Detonation Properties. [Pg.185]

Flow calorimetric measurements of the excess enthalpy of a steam + n-heptane mixture over the temperature range 373 to 698 K and at pressures up to 12.3 MPa are reported. The low pressure measurements are analysed in terms of the virial equation of state using an association model. An extension of this approach, the Separated Associated Fluid Interaction Model, fits the measurements at high pressures reasonably well. [Pg.446]

The PVT properties of aqueous solutions can be determined by direct measurements or estimated using various models for the ionic interactions that occur in electrolyte solutions. In this paper a review will be made of the methods presently being used to determine the density and compressibility of electrolyte solutions. A brief review of high-pressure equations of state used to represent the experimental PVT properties will also be made. Simple additivity methods of estimating the density of mixed electrolyte solutions like seawater and geothermal brines will be presented. The predicted PVT properties for a number of mixed electrolyte solutions are found to be in good agreement with direct measurements. [Pg.581]

A brief review is made of the methods that are currently being used to determine the density (p) and compressibility (6) of electrolyte solutions as a function of pressure. The high pressure equations of state used to represent these properties are also discussed. The linear secant bulk modulus [K = Ppp/(pP - p )] equation of state... [Pg.617]

Constant (3- Equation of State. See under "Detonation (and Explosion), Equations of State Used in ... [Pg.186]

Cook equation of state, using covolume approximation) 63-4 (Other coyolume equations of state) 65 (Jones, Jones-Miller and Lennard-Jones equations of state) 66 (Cot-trell-Paterson equation of state) 12aj) W. Fickett W.W. Wood, Physics of Fluids 1, 528(1958 (A Detonation-Product Equation of State Observed from Hydrodynamic Data)... [Pg.297]

Unlike the relation between brisance and PCJ, expl strength is not readily related to some detonation characteristic of the explosive. Attempts to relate strength to detonation energy are not wholly successful. Relative strength, based on ballistic mortar tests, correlates rather well with computed nRT, where n T are the computed moles of gas and detonation temp of the explosive, and R is the gas constant. Although n T can differ appreciably with the equation of state used in the computation, it appears that ratios of nRT (at least for similar explosives) do not suffer from this drawback... [Pg.580]

Optimizing solvents and solvent mixtures can be done empirically or through modeling. An example of the latter involves a single Sanchez-Lacombe lattice fluid equation of state, used to model both phases for a polymer-supercritical fluid-cosolvent system. This method works well over a wide pressure range both volumetric and phase equilibrium properties for a cross-linked poly(dimethyl siloxane) phase in contact with CO2 modified by a number of cosolvents (West et al., 1998). [Pg.74]

For detailed references and a brief general discussion of other equations of state used in condensed-phase detonation problems, see S. J. Jacobs, ARS (Am. Rocket Soc. J.) 30, 151 (1960). [Pg.1]

The molar Helmhotz energy a is obtained from an equation of state using the relation (da / dv)T X= P All derivatives in these two determinants can be obtained from an equation... [Pg.23]

Some of these ambiguities can be partially solved using a simple approach recently proposed by Gamier et al. [62], The sublimation pressure of a solid can be estimated using experimental fusion properties and the vaporization enthalpy derived from the equation of state. Using the Clapeyron equation P b can be approximated by ... [Pg.49]

General relativity magnifies this effect, but at the same time reduces the mass of the homologous core at bounce and forces the shock to unfavourably traverse more stellar material on its way out of the core. The equation of state used in our astrophysical simulations has the simple form [19]... [Pg.356]

Repeat Exercise 4-4. Use the Soave-Redlich-Kwong equation of state. Use values of zero for the binary interaction coefficients. [Pg.145]

EXAMPLE 15-2 Calculate the compositions of the gas and liquid when the mixture with composition given below is brought to equilibrium at 160°F and 1000 psia. Use the Peng-Robinson equation of state. Use binary interaction coefficients of 0.02 for meth-ane-n-butane, 0.04 for methane-n-decane, and 0.0 for n-butane-n-decane. [Pg.431]

RT = (p+ a/v2) - (v - b), it is the quantity b which corresponds to four times the square root of the space occupied by the molecules themselves (Ref 6). The classical equation of state used by ballisticians and known as the Noble - Abel equation of state is written... [Pg.333]

When applying an equation of state to both vapor and liquid phases, the vapor-liquid equilibrium predictions depend on the accuracy of the equation of state used and, for multicomponent systems, on the mixing rules. Attention will be given to binary mixtures of hydrocarbons and the technically important nonhydrocarbons such as hydrogen sulfide and carbon dioxide -Figures 6-7. [Pg.111]

The excess chemical potential of a hard-sphere fluid can be calculated on the basis of an equation of state using the expressions17... [Pg.335]


See other pages where Equations of state using is mentioned: [Pg.399]    [Pg.340]    [Pg.61]    [Pg.131]    [Pg.36]    [Pg.123]    [Pg.180]    [Pg.277]    [Pg.286]    [Pg.227]    [Pg.44]    [Pg.52]    [Pg.92]    [Pg.10]    [Pg.10]    [Pg.238]    [Pg.127]    [Pg.322]   
See also in sourсe #XX -- [ Pg.235 , Pg.236 , Pg.237 , Pg.238 , Pg.239 ]




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