Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Real liquids

The standard state of a substance in a condensed phase is the real liquid or solid at 1 atm and T. [Pg.367]

For species present as gases in the actual reac tive system, the standard state is the pure ideal gas at pressure P°. For liquids and solids, it is usually the state of pure real liquid or solid at P°. The standard-state pressure P° is fixed at 100 kPa. Note that the standard states may represent different physical states for different species any or all of the species may be gases, liquids, or solids. [Pg.542]

The question arises as to how useful atomistic models may be in predicting the phase behaviour of real liquid crystal molecules. There is some evidence that atomistic models may be quite promising in this respect. For instance, in constant pressure simulations of CCH5 [25, 26] stable nematic and isotropic phases are seen at the right temperatures, even though the simulations of up to 700 ps are too short to observe spontaneous formation of the nematic phase from the isotropic liquid. However, at the present time one must conclude that atomistic models can only be expected to provide qualitative data about individual systems rather than quantitative predictions of phase transition temperatures. Such predictions must await simulations on larger systems, where the system size dependency has been eliminated, and where constant... [Pg.57]

In classical homogenous catalysis, an organic compound, i.e., a real liquid phase (a solvent) dissolves all of the reactants, catalysts, and products. The role of the solvent is underlined by the fact that it has to be separated from the reaction products by an additional and costly step, for example by distillation. [Pg.107]

A wide range of values (one decade ) could be obtained using correlations as well as using different experimental methods [34, 38, 43]. As for solubility, diffusion coefficient at infinite dilution should be determined experimentally using the real liquid phase. Experimental methods are, however, more complex to carry out and correlations are widely used. [Pg.1526]

Our development has assumed temperature independent force constants. In real liquids, however, there is a small temperature dependence of frequencies and force constants due to anharmonicities, lattice expansion, etc. The incorporation of these effects into the theory is treated in later sections. [Pg.152]

MSE.I8. I. Prigogine, The molecular theory of surface tension, in Cavitation in Real liquids, R. Davies, ed., Elsevier, Amsterdam, 1964, pp. I47-I63. [Pg.52]

At flow rates greater than about 100 cm /s, the frequency becomes essentially constant at a value of about 20 s close to the value for bubble formation in real liquids (B4, H7). The volume of bubbles formed, however, is generally less than Qjf due to leakage of gas into the dense phase (N3). The length of jets, when these occur, feeding forming bubbles is correlated (M12) by the equation... [Pg.330]

However, as accurate experimental data were accumulated, it has become apparent that these earlier theories of rodlike polymers fail to describe quantitatively the behavior of real liquid-crystalline polymers, which are not completely rigid but more or less flexible. [Pg.90]

Liquids. For a long time, the study of infrared absorption by liquids and solutions has been a convenient way of determining rotovibrational spectra. The goal has often been to just determine peak frequencies, without paying much attention to the band shapes. In more recent years, attention has been devoted to a study of the shapes of vibrational bands and the dynamics of the molecules in the liquid. Only a crude understanding of the dynamics exists which is based on often highly simplified models of real liquids. [Pg.374]

Reference type of ww type of treatment system no, and type of ozone reactors (operating pressure) ozone production capacity nominal// real liquid flow-rate ozone yield coefficient Y(OJM) (M = COD) investment ozonation stage only specific costs (without annuity) remarks... [Pg.31]

Calculation of the Bubble-Point Pressure of a Real Liquid... [Pg.359]

Compositions and Quantities of the Equilibrium Gas and Liquid Phases of a Real Solution — Calculation of the Bubble-Point Pressure of a Real Liquid—Calculation of the Dew-Point Pressure of a Real Gas Flash Vaporization 362... [Pg.558]

CAVITATION. Cavities may form, grow, and collapse in a liquid when variational tensile stresses are superimposed on the prevailing ambieni pressure. Pure liquids have theoretical tensile strengths, which are estimated on various grounds to be of the order of 300 to 1500 atmospheres (bars), but the observed tensile strengths or real liquids are much lower. It is presumed, iherefore, that the observed tensile strength is a measure of the stress required to enlarge the minute cavities, or cavitation nuclei, which already exist in (he liquid rather than the stress required to form new interior surfaces. [Pg.308]

The intermolecular potential consists of the sum of Eqs. (176), (177), (178), and (179). This simulation was done for 216 and 512 molecules but again only the autocorrelation functions for 512 molecules are discussed here. This potential is the strongest angular dependent potential we considered. The results from this potential indicate that it is slightly stronger than that in real liquid carbon monoxide. For example the mean square torque/TV2), for this simulation is 36 x 10-28 (dyne-cm)2 51 and the experimental value is 21 x 10-28 (dyne-cm)2. If this potential is taken seriously, then it should be pointed out that this small discrepancy in torques could be easily removed by using a smaller quadrupole moment. This would be a well justified step since experimental quadrupole moments for carbon monoxide range from 0.5 x 10-26 to 2.43 x 10-26 esu.49... [Pg.69]

In comparing our systems to real liquids of carbon monoxide and nitrogen, we are assuming implicitly that these real liquids behave like classical systems of rigid rotors. That is, quantum effects are relatively small. The usual criteria that have to be satisfied for this to be true are ... [Pg.72]

The molecules must be predominantly in their ground state vibrational level, i.e., h(oec/KT < 1, where c is the velocity of light and energy separation of successive levels in wave numbers. For carbon monoxide at68°K with p = 0.8558 g/ccand a>e = 2.170 x 103 cm-1,45 the above factors are 2 x 10"1, 5 x 10 2, and 5 x 101, respectively. Therefore, to a first approximation real liquid carbon monoxide at this temperature and density behaves classically, and our comparisons will be justified. [Pg.72]

The main contributions to the frequency-time correlation function are assumed to be, as in the earlier works [123, 124], from the vibration-rotation coupling and the repulsive and attractive parts of the solvent-solute interactions. In several theories, the (faster) repulsive and the (slower) attractive contributions are assumed to be of widely different time scales and are treated separately. However, this may not be true in real liquids because the solvent dynamic interactions cover a wide range of time scales and there could be a considerable overlap of their contributions. The vibration-rotation coupling contribution takes place in a very short time scale and by neglecting the cross-correlation between this mechanism and the atom-atom forces, they... [Pg.170]

A conglomerate in real liquid crystalline phases was first observed in the smectic phase of a rod-shaped mesogen with two stereogenic centers in its tail [42], We used a racemic mixture which was supposed not to electrically switch. Evidence for conglomerate formation was provided by clear electro-optic switching and texture observation under a polarizing microscope domains with stripes, which themselves display fine stripes. These stripes are tilted in two different directions with respect to the primary stripes. This is a still very rare example now that fluid soft matter is known to resolve spontaneously into a three-dimensional conglomerate. [Pg.312]

In a nonflow process the energy stored in a fluid by compression is represented by Jl P dv. Each small increment of gas compressed dv, multiplied by the pressure p, and added to all other small increments equals the energy stored in the gas. If the fluid is incompressible, such as a liquid, dv is zero. For any real liquid, the compressibility is small, and the stored pressure energy is negligible. For a gas or a vapor, this store of energy may be very appreciable. [Pg.399]

In the case of a real liquid in an open channel, it is necessary to differentiate between the behavior at subcritical and supercritical velocities. Subcritical flow in a rectangular channel has been investigated experimentally and has been found to conform fairly well to ideal conditions, especially within the first part of the bend [44], As the flow continues around the bend, the velocity distribution becomes complicated by the phenomenon of spiral flow, which for open channels is analogous to the secondary counterrotating currents found at bends in closed pipes. [Pg.498]

We shall discuss first the concept of the ideal liquid mixture (section 32.2) [i.e. one whose vapour pressure characteristics are such that they follow Raoult s Law (see below)] and contrast this with a real liquid mixture [i.e. one where non-ideal behaviour is exhibited and for which Raoult s Law is no longer obeyed]. We can then compare this concept of an ideal and real liquid mixture with that of ideal and real gases (Frame 31) showing that the ideas are fairly similar in nature and that parallels can be drawn and applied to their distinction and also that their definitions refer to limiting laws which apply. [Pg.94]

Here Raoult s law acts as the limiting demarcation criterion between ideal and real or non-ideal liquid mixtures. As Figure 32.4(a) indicates, in practice, non-ideal (real) liquid mixtures do not show linear behaviour but their vapour pressure deviates from (i.e. above or below) the line AB. [Pg.96]

Ideal Liquid Mixtures Real Liquid Mixtures... [Pg.98]

What we would like to be able to do is to determine for a real (i.e. non-ideal) liquid mixture what effective concentration we need to use in order to adapt the ideal equation (39.1) to give the same chemical potential as the real liquid mixture. Now, for gases, we have established (Frame 38) that ... [Pg.126]


See other pages where Real liquids is mentioned: [Pg.57]    [Pg.115]    [Pg.105]    [Pg.110]    [Pg.36]    [Pg.168]    [Pg.1523]    [Pg.1525]    [Pg.337]    [Pg.423]    [Pg.270]    [Pg.197]    [Pg.63]    [Pg.231]    [Pg.932]    [Pg.937]    [Pg.61]    [Pg.117]    [Pg.81]    [Pg.293]    [Pg.256]    [Pg.406]    [Pg.211]    [Pg.110]    [Pg.126]   
See also in sourсe #XX -- [ Pg.201 ]




SEARCH



Degradation in Real Liquid Environments

Physical description of a real liquid interface

Real Behavior of Liquid Mixtures

Real and ideal liquids

Real liquid mixed systems

© 2024 chempedia.info