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Temperature only function

The coefficients B, C, D, etc for each particular gas are tenned its second, third, fourth, etc. vihal coefficients, and are functions of the temperature only. It can be shown, by statistical mechanics, that 5 is a function of the interaction of an isolated pair of molecules, C is a fiinction of the simultaneous interaction of tln-ee molecules, D, of four molecules, etc., a feature suggested by the fomi of equation (A2.1.54). [Pg.355]

Since 1/P) should be a function of temperature only, character-... [Pg.89]

Expansion from high to low pressures at room temperature cools most gases. Hydrogen is an exception in that it heats upon expansion at room temperature. Only below the inversion temperature, which is a function of pressure, does hydrogen cool upon expansion. Values of the Joule-Thorns on expansion coefficients for hydrogen have been tabulated up to 253 MPa (36,700 psi) (48), and the Joule-Thorns on inversion curve for i7n -hydrogen has been determined (49,50). [Pg.414]

Equations 10 and 11 are known as vitial expansions, and the coefficients (7, D. .. and B, C, D,. .. are called virial coefficients. For a given substance, these coefficients are functions of temperature only (1 3). [Pg.234]

These equations clearly show that for an ideal gas U, H, Cp, and Cy are functions of temperature only and are independent of f and V The entropy of an ideal gas, however, is a func tion of both T and f or of both T and V... [Pg.517]

The right-hand side of this equation is a function of temperature only for given reactions and given standard states. Convenience suggests setting it equal to In Kj whence... [Pg.542]

The total derivative is appropriate here because property changes of reaction are functions of temperature only. In combination with Eq. (4-343) this gives... [Pg.543]

If the feed flows countercurrent to the air, as is the case when drying granulated sugar, exhaust temperature does not respond to variations in product moisture. For these diyers, product moisture can better be regulated by controlhng its temperature at the point of discharge. Conveyor-type diyers are usually divided into a number of zones, each separately heated with recirculation of air which raises its wet-bulb temperature. Only the last two zones may require indexing of exhaust-air temperature as a function of AT... [Pg.751]

Fig. 8.10. The displacive f.c.c. —> b.c.c. transformation in iron the volume of martensite produced is a function of temperature only, and does not depend on time. Note that the temperature at which martensite starts to form is labelled (martensite start) the temperature at which the martensite transformation finishes is labelled Mf (martensite finish). Fig. 8.10. The displacive f.c.c. —> b.c.c. transformation in iron the volume of martensite produced is a function of temperature only, and does not depend on time. Note that the temperature at which martensite starts to form is labelled (martensite start) the temperature at which the martensite transformation finishes is labelled Mf (martensite finish).
The well-known difficulty with batch reactors is the uncertainty of the initial reaction conditions. The problem is to bring together reactants, catalyst and operating conditions of temperature and pressure so that at zero time everything is as desired. The initial reaction rate is usually the fastest and most error-laden. To overcome this, the traditional method was to calculate the rate for decreasingly smaller conversions and extrapolate it back to zero conversion. The significance of estimating initial rate was that without any products present, rate could be expressed as the function of reactants and temperature only. This then simplified the mathematical analysis of the rate fianction. [Pg.29]

Since the dithiocarbatnyl end groups 8 are thermally stable but pholochemically labile at usual polymerization temperatures, only photo-initiated polymerizations have the potential to show living characteristics. However, various disulfides, for example, 9 and 10, have been used to prepare end-functional polymers37 and block copolymers38 by irreversible chain transfer in non-living thermally-initiated polymerization (Section 7.5.1). [Pg.463]

If we truncate Eqs. (63) and (64) after the first terms, and assume as before that the partial volume of the solute is a function of temperature only, we obtain the equation of Krichevsky and Ilinskaya (K5) 5... [Pg.169]

Equations (76) and (77) contain two constants, A and B, which, for any binary pair, are functions of temperature only. These equations appear to be satisfactory for accurately representing activity coefficients of nonpolar binary mixtures from the dilute region up to the critical composition. As examples, Figs. 12 and 13 present typical results of data reduction for two systems in these calculations, the reference pressure Pr was set equal to zero. [Pg.177]

For an incompressible fluid, the density variation with temperature is negligible compared to the viscosity variation. Hence, the viscosity variation is a function of temperature only and can be a cause of radical transformation of flow and transition from stable flow to the oscillatory regime. The critical Reynolds number also depends significantly on the specific heat, Prandtl number and micro-channel radius. For flow of high-viscosity fluids in micro-channels of tq < 10 m the critical Reynolds number is less than 2,300. In this case the oscillatory regime occurs at values of Re < 2,300. [Pg.163]

Activation parameters are always computed from rate constants, and their errors are functions of errors in logk. If the reaction is followed at two temperatures only, the pertinent formulas read (142) ... [Pg.432]

Eq. (18) is now a function of temperature only. It can be solved by any trial and error procedure such as successive substitution or regula falsi (Gerald (1978)). Having obtained the optimum temperature from Eq. (18), the corresponding minimum time can be calculated from Eq. (17). [Pg.325]

Since a — L/La where Lo is a function of pressure and temperature only. [Pg.489]

Figure 3a shows the spectra of CO adsorbed at room temperature on a typical Cr(II)/Si02 sample. At low equilibrium pressure (bold black curve), the spectrum shows two bands at 2180 and 2191 cm Upon increasing the CO pressure, the 2191 cm component grows up to saturation without frequency change. Conversely, the 2180 cm component evolves into an intense band at 2184 cm and a shoulder at 2179 cm The bands at 2191, 2184, and 2179 cm which are the only present at room temperature for pressures lower than 40 Torr, are commonly termed the room temperature triplet and are considered the finger print of the Cr(ll)/Si02 system (grey curve in Fig. 3). A new weak band at around 2100 cm appears at room temperature only at higher CO pressure. As this peak gains intensity at lower temperature, it will be discussed later. The relative intensity of the three components change as a function of the OH content (i.e., with the activation temperature and/or the activation time) [17]. Figure 3a shows the spectra of CO adsorbed at room temperature on a typical Cr(II)/Si02 sample. At low equilibrium pressure (bold black curve), the spectrum shows two bands at 2180 and 2191 cm Upon increasing the CO pressure, the 2191 cm component grows up to saturation without frequency change. Conversely, the 2180 cm component evolves into an intense band at 2184 cm and a shoulder at 2179 cm The bands at 2191, 2184, and 2179 cm which are the only present at room temperature for pressures lower than 40 Torr, are commonly termed the room temperature triplet and are considered the finger print of the Cr(ll)/Si02 system (grey curve in Fig. 3). A new weak band at around 2100 cm appears at room temperature only at higher CO pressure. As this peak gains intensity at lower temperature, it will be discussed later. The relative intensity of the three components change as a function of the OH content (i.e., with the activation temperature and/or the activation time) [17].
Influence of temperature on the reaction rate. It is usually assumed that the rate constant is a function of temperature only, expressed by the Arrhenius equation ... [Pg.279]

Here, k is the reaction rate constant, which is a function of temperature only Ca, Cb are the concentrations of the reactants A, B (moles/volume) a is the order of reaction, with respect to A (3 is the order of reaction, with respect to B (a + p) is the overall order of the reaction. [Pg.53]

The damage effects from an explosion depend highly on whether the explosion results from a detonation or a deflagration. The difference depends on whether the reaction front propagates above or below the speed of sound in the unreacted gases. For ideal gases the speed of sound or sonic velocity is a function of temperature only and has a value of 344 m/s (1129 ft/s) at 20°C. Fundamentally, the sonic velocity is the speed at which information is transmitted through a gas. [Pg.253]

The electronic heat capacity for the free electron model is a linear function of temperature only for T Tp = p / kp. Nevertheless, the Fermi temperature Tp is of the order of 105 K and eq. (8.46) holds for most practical purposes. The population of the electronic states at different temperatures as well as the variation of the electronic heat capacity with temperature for a free electron gas is shown in Figure 8.20. Complete excitation is only expected at very high temperatures, T>Tp. Here the limiting value for a gas of structureless mass points 3/2/ is approached. [Pg.254]


See other pages where Temperature only function is mentioned: [Pg.607]    [Pg.359]    [Pg.314]    [Pg.149]    [Pg.403]    [Pg.494]    [Pg.519]    [Pg.451]    [Pg.441]    [Pg.469]    [Pg.1128]    [Pg.12]    [Pg.205]    [Pg.372]    [Pg.166]    [Pg.805]    [Pg.9]    [Pg.277]    [Pg.387]    [Pg.12]    [Pg.111]    [Pg.112]    [Pg.13]    [Pg.136]    [Pg.140]   
See also in sourсe #XX -- [ Pg.571 ]




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