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Mixture pressure

Figure B-2. Psychrometric chart atmospheric air, mixture pressure (barometric) 29.921 in. Hg. (From Short, Kent and Walls, Pressure-Enthalpy Otarts for Selected Engineering Substances. Gulf Publishing Company, Houston, TX, 1970.)... Figure B-2. Psychrometric chart atmospheric air, mixture pressure (barometric) 29.921 in. Hg. (From Short, Kent and Walls, Pressure-Enthalpy Otarts for Selected Engineering Substances. Gulf Publishing Company, Houston, TX, 1970.)...
Relative humidity is usually considered only in connection with atmospheric air, but since it is unconcerned with the nature of any other components or the total mixture pressure, the term is applicable to vapor content in any problem. The saturated water vapor pressure at a given temperature is always known from steam tables or charts. It is the existing partial vapor pressure which is desired and therefore calculable when the relative humidity is stated. [Pg.634]

At higher pressures only Raman spectroscopy data are available. Because the rotational structure is smoothed, either quantum theory or classical theory may be used. At a mixture pressure above 10 atm the spectra of CO and N2 obtained in [230] were well described classically (Fig. 5.11). For the lowest densities (10-15 amagat) the band contours have a characteristic asymmetric shape. The asymmetry disappears at higher pressures when the contour is sufficiently narrowed. The decrease of width with 1/tj measured in [230] by NMR is closer to the strong collision model in the case of CO and to the weak collision model in the case of N2. This conclusion was confirmed in [215] by presenting the results in universal coordinates of Fig. 5.12. It is also seen that both systems are still far away from the fast modulation (perturbation theory) limit where the upper and lower borders established by alternative models merge into a universal curve independent of collision strength. [Pg.182]

A consequence of mechanical equilibrium in a perfect gas mixture is that the pressures developed by each species sum to give the mixture pressure. This is known as Dalton s law, with the species pressure called the partial pressure, / , ... [Pg.26]

This is an important relationship between the mole fraction and the ratio of partial and mixture pressures. [Pg.26]

Sometimes mole fractions are called volume fractions. The volume that species i would occupy if allowed to equilibrate to the mixture pressure is... [Pg.26]

By Dalton s law, Equation (2.9), the mixture pressure, p, is Y i= Pi- The ternl Y I PiVjhj is sometimes considered to be a heat flow rate due to the transport of enthalpy by the species. (This is not the same as q" arising from VT which is called the Dufour effect and is generally negligible in combustion.) With the exception of the enthalpy diffusion term, all the sums can be represented in mixture properties since ph = Ya i Pihi However, it is convenient to express the enthalpies in terms of the heat of formation and specific heat terms, and then to separate these two parts. [Pg.63]

Natural gas mixtures, pressure-volume-temperature (PVT) behavior of, 12 370 Natural gas production, 12 372-378 13 592 nitrogen in, 17 287 Natural gas reserves, 12 366-369 estimate of undiscovered, 12 368 Natural gas reservoirs, 12 372 Natural graphite, 12 771-799 analytical and test methods for, 12 786-790... [Pg.613]

P = water vapor pressure, air pressure, or total mixture pressure (water plus air) M = molecular weight of the vapor phase... [Pg.186]

Phase Diagrams of Two-Component Mixtures — Pressure-Volume Diagram for a Two-Component Mixture — Composition Diagrams... [Pg.554]

There are many methods of obtaining explosion-limit data. In general, they involve rapid heating of a mixture, rapid mixing at a known temperature, or changing the mixture pressure at a constant temperature. The results are in most cases self-consistent but rarely agree from method to method. Jost 31) discusses most of the methods and compares results obtained with some of them. Here, only those methods most commonly used in kinetics studies are discussed and critically evaluated. [Pg.102]

For our example, if the mixture pressure is taken as 4 bar, we can develop the following table ... [Pg.161]

Figure 8.15 The effect of stage-cut on the separation of a 50/50 feed gas mixture (pressure ratio, 20 membrane selectivity, 20). At low stage-cuts a concentrated permeate product, but only modest removal from the residue, can be obtained. At high stage-cuts almost complete removal is obtained, but the permeate product is only slightly more enriched than the original feed... Figure 8.15 The effect of stage-cut on the separation of a 50/50 feed gas mixture (pressure ratio, 20 membrane selectivity, 20). At low stage-cuts a concentrated permeate product, but only modest removal from the residue, can be obtained. At high stage-cuts almost complete removal is obtained, but the permeate product is only slightly more enriched than the original feed...
Are there any differences in operation—such as the nature of the feed mixture, pressure, temperature, etc., that may affect the scaleup of HETP to the new design ... [Pg.574]

The track at the bottom shows the output signal of a pressure transducer monitoring the gas mixture pressure inside P. Obviously, there is no ignition of the Fl2-air test mixture. To ensure its ignitability, the H2-air mixture has... [Pg.509]

FIGURE 14-g For ideal gas mixtures, pressure fraction of a gas is equal to its mole fraction. [Pg.792]

The autoclave is then gradually cooled, first to room temperature, and then to -78° in an acetone-dry ice mixture. Pressure is then released through a cold trap. The IR spectrum shows only the two C—O stretching bands of Ru(CO)s at 2042 and 1996 cm (observed values in acetone solution). The yield is practically quantitative. This solution is used directly in the following steps. Note In other solvents, like hexane or diethyl ether, the reaction is identical to that in acetone the time required to the completion of the reaction can vary considerably, however. [Pg.166]

Example 8 Calculation of Humidity and Wet-Bulb Condition A dryer exhaust which can be taken as an air-water mixture at 70°C (343.15 K) is measured to have a relative humidity of 25 percent. Calculate the humidity parameters and wet-bulb conditions for the mixture. Pressure is 1 bar (100,000 Pa). [Pg.1336]

Raising the gas mixture pressure causes the mixture to ignite at lower temperatures as shown by Ref. ... [Pg.1113]

The nine components of these three vectors form a symmetric pressure tensor, P, hence the mixture pressure yields ... [Pg.264]

In a set of intermediate steps, the evolution of the mixture pressure and velocity components are calculated. The variable density form of the Navier-Stokes equations are split into two intermediate steps. [Pg.1059]

Equations (65) and (66) show that the process of creating supersaturation within the droplets is much slower than in homogeneous mixtures (i.e., at pressures above the critical mixture pressure). Increase of the solute concentration from Cco to 2cco is observed after 0.206tvap> which for t ap = 0.125 s... [Pg.136]

Two separate models based on Dow Advanced Continuous Simulation Language (DACSL) were used in these studies. The first model used laboratory data and parameter estimation to determine the Arrhenius constants for two desired and eight undesired reactions in a process. The second model used the Arrhenius constants, heats of reaction, different physical properties, and reactor parameters (volume, heat transfer properties, jacket control parameters, jacket inlet temperature) to simulate the effect of reaction conditions (concentration, set temperature, addition rate) on the temperature of the reaction mixture, pressure and gas flow rates in the reactor, yield, and assay of the product. The program has been successfully used in two scale-ups where the optimum safe operating conditions, effect of various possible failures, and control of possible abnormal conditions were evaluated. [Pg.93]

In the proposed vapor phase processes for organic acid synthesis, carbon monoxide is passed with the vaporized aliphatic alcohol over catalysts similar in nature to those employed in the pressure synthesis of higher alcohols from hydrogen-carbon monoxide mixtures. Pressures on the order of 200 atmospheres are employed. Temperatures of about 200° to 300° C. are preferred but it is necessary to use somewhat higher ones in order to obtain sufficient reaction. Mixtures of the oxides of zinc and chromium or copper, promoted with alkali or alkaline earth oxides, are suitable catalysts for the formation of carbon-carbon linkages.97 Catalysts composed of an alkali, chromium, and molybdenum have been claimed for the synthesis of mixtures of higher alcohols, aldehydes, acids, esters, etc., from carbon monoxide and vaporized aliphatic alcohols as methanol, ethanol, etc., at temperatures of about 420° C. and a pressure of 200 atmospheres.98... [Pg.91]


See other pages where Mixture pressure is mentioned: [Pg.1248]    [Pg.139]    [Pg.145]    [Pg.18]    [Pg.199]    [Pg.377]    [Pg.41]    [Pg.255]    [Pg.302]    [Pg.8]    [Pg.114]    [Pg.598]    [Pg.404]    [Pg.184]    [Pg.51]    [Pg.6]    [Pg.1071]    [Pg.170]    [Pg.816]    [Pg.114]    [Pg.1440]    [Pg.467]    [Pg.407]   
See also in sourсe #XX -- [ Pg.267 ]




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