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Saturation relative

T — T (4) the ratio of the solute concentration and the equiUbrium concentration, c A, which is known as relative saturation or (5) the ratio of the difference between the solute concentration and the equiUbrium concentration to the equiUbrium concentration, s — [c — c which is known as relative supersaturation. This term has often been represented by O s is used here because of the frequent use of O for iaterfacial energy or surface tension and for variance ia distribution functions. [Pg.341]

Temperature and Humidity of Rich Gas Cooling and consequent dehumidification of the feed gas to an absorption tower can be very beneficial. A high humidity (or relative saturation with solvent) limits the capacity of the gas phase to take up latent heat and therefore is unfavorable to absorption. Thus, dehumidification of the inlet gas prior to introducing it into the tower is worth considering in the design of gas absorbers with large heat effects. [Pg.1359]

The simplest mode of IGC is the infinite dilution mode , effected when the adsorbing species is present at very low concentration in a non-adsorbing carrier gas. Under such conditions, the adsorption may be assumed to be sub-monolayer, and if one assumes in addition that the surface is energetically homogeneous with respect to the adsorption (often an acceptable assumption for dispersion-force-only adsorbates), the isotherm will be linear (Henry s Law), i.e. the amount adsorbed will be linearly dependent on the partial saturation of the gas. The proportionality factor is the adsorption equilibrium constant, which is the ratio of the volume of gas adsorbed per unit area of solid to its relative saturation in the carrier. The quantity measured experimentally is the relative retention volume, Vn, for a gas sample injected into the column. It is the volume of carrier gas required to completely elute the sample, relative to the amount required to elute a non-adsorbing probe, i.e. [Pg.35]

An important variable that determines the size of a given desiccant bed is the relative saturation of the inlet gas. This variable is the driving force that affects the transfer of water to the adsorbent. If saturated gas (100% relative humidity) is being dried, higher useful capacities can be expected for most desiccants than when drying partially saturated gases. However, in most field gas dehydration installations the inlet gas is samrated with water vapor and this is not a variable that must be considered. [Pg.235]

In a volume of 1 m3 of a mixture of air and acetone vapour, the temperature is 303 K and the total pressure is 100 kN/m2. If the relative saturation of the air by acetone is 40 per cent, what mass of activated carbon must be added to the space so that at equilibrium the value is reduced to 5 per cent at 303 K ... [Pg.243]

If 1.6 kg carbon is added, what is relative saturation of the equilibrium mixture assuming the temperature to be unchanged The vapour pressure of acetone at 303 K is 37.9 kN/m2 and the adsorption equilibrium data for acetone on carbon at 303 K are ... [Pg.243]

The sixth class of green emitters is metal organic complexes. Alq3 was the first green emitter. Alq3 emission exhibits relatively saturated green color (CIE 1931 coordinates (0.32,0.55)) and so far, it is still one of the best green emitters available. [Pg.343]

Equation (99) implies that it is often possible to specify intervals or approximate values for the scaled elasticities in terms of relative saturation, even when detailed kinetic information is not available. For example, as a rule of thumb, the substrate concentration can often be considered to be on the order of the Km value. As the scaled elasticities, by means of the control coefficients, can be directly translated into a systemic response, it is possible to utilize such heuristic arguments to acquire an initial approximation of global network properties. [Pg.180]

If 1.6 kg carbon is added, what is relative saturation of the equilibrium mixture assuming the temperature to... [Pg.1182]

The relative permeability is difficult to quantify. It usually is estimated on the basis of laboratory experiments, as a function of relative saturation. In three-phase NAPL-water-air systems, each relative permeability is dependent on the relative saturation of each of the phases. Modeling based on empirical considerations can be employed. For example. Blunt (2000) discusses a model to estimate three-phase relative permeability, based on saturation-weighted interpolation of two-phase relative permeabilities. The model accounts for the trapping of the NAPL and air (gas)... [Pg.239]

For a fixed coefficient of friction p. and a fixed dimensionless shear rate K, the measurement of the power consumption per unit volume of the moist powder mass is proportional to the cohesive stress Uc- Thus, if the granulating liquid is added to the powder mass at a constant rate, the power consumption profile describes in a first approximation the cohesive stress (Tc as a function of the relative saturation S of the void space between the particles (Fig. 5). [Pg.209]

The oxygen and NOx storage phenomena are characterized by the maximum effective storage capacities 4temperature-dependent relative saturation coverages J/eq(T) and kinetic constants k/ T) determining the dynamics of the... [Pg.151]

Relative humidity or relative saturation is the ratio of the prevailing humidity to the saturation humidity at the same temperature, or the ratio of the partial pressure to the vapor pressure expressed as a percentage,... [Pg.231]

For a fractional conversion a of toluene of 0.1, Table 4.2 shows how / (which is the same as the mole fraction of chlorine in the outlet gas) and (1 - /j (the fractional conversion of the chlorine) vary with the superficial gas velocity u0 over the range 0.01 to 0.05 m/s, as required in the problem. Table 4.2 also shows the concentration of the dissolved chlorine in the bulk liquid Car calculated from equation E. Shown also is the relative saturation of the liquid CqXJCqXL, where Car is the saturation chlorine concentration in the bulk liquid at the operating pressure of the reactor, i.e. 1.0 bar. [Pg.215]

If equilibrium has not been reached between a mixture of components, the condition is referred to as partial saturation. At partial saturation the gas mixture obeys real gas laws. There are several ways to express the concentration of a vapor in a mixture of gases. Most often, weight or mole fraction is used. Other definitions are relative saturation (relative humidity), molal saturation (molal humidity) and absolute saturation (absolute humidity). [Pg.18]

The percent saturation is never greater than the relative saturation except at saturated conditions or at zero percent saturation (where % saturation = % RH). [Pg.19]

Rs = relative saturation RFi = relative humidity T = temperature, °F tw = wet-bulb temperature, °F U = internal energy, Btu/lb... [Pg.33]

Enzymes as different as yeast alcohol oxidase, mushroom polyphenol oxidase, and horse-liver alcohol dehydrogenase demonstrated vastly increased enzymatic activity in several different solvents upon an increase in the water content, which always remained below the solubility limit (Zaks, 1988b). While much less water was required for maximal activity in hydrophobic than in hydrophilic solvents, relative saturation seems to be most relevant to determining the level of catalytic activity. Correspondingly, miscibility of a solvent with water is not a decisive criterion upon transition from a monophasic to a biphasic solvent system, no significant change in activity level was observed (Narayan, 1993). Therefore, the level of water essential for activity depends more on the solvent than on the enzyme. [Pg.346]

When the dyeing equilibrium is reached, the relative saturation value Vrei indicates the degree of levelness which can be expected during dye absorpion the higher. S rci the better the levelness. For similar AVei for different dyeings a similar course of the dyeing process can be assumed. [Pg.413]

The following are the results a series of simulation calculations for the determination of the relative saturation of the masonry with hydrogen cyanide based on the assumption that similar concentrations of hydrogen cyanide are used in all cases. In so doing, a distinction is made between two sets of circumstances ... [Pg.227]

In former editions of this expert report, I have used the equations determined in chapter 6.7.4. to calculate the relative saturation of masonry cyclically exposed to hydrogen cyanide. However, after using several approaches on exactly how to do it, which lead to sometimes quite different results,482 1 decided to refer to this equation only in order to establish the time it takes for masonry to reach its maximum saturation or a quasi-constant concentration (20 days and 20 daily cycles, respectively). In this edition, the quasi-stationary concentration in masonry were calculated iteratively using Fick s law of diffusion 483... [Pg.228]

Figure 6.24 (a) and (b) show how the relative permeabilities of oil and water can vary with relative saturation of the pores, and with wettability. This figure also illustrates the fact that the relative permeability of a fluid will become zero while the other fluid still has a finite saturation. This is because a significant amount of either fluid can become immobilized and will not be displaced by the other fluid. The nature and extent of this immobilization depends upon the same factors as just listed for permeability. [Pg.198]

The solubility of magnesium sulfite hexahydrate in water with the addition of magnesium sulfate was accurately predicted by the LCM for 0-6 molal (29). The relative saturation of the magnesium sulfite hexhydrate was predicted within 10 percent error at 40 and 50 C, and within 20 percent error at 60 C. [Pg.234]

Figure 2 (right). Comparison of SDM Davies Technique and LCM in Predicting Gypsum Relative Saturation with the Addition of Sodium Sulfate. Data from Hill and Wills (25). [Pg.235]

Figure 2. Argon adsorption isotherms for microporous and nonmicroporous catalyst supports. The normalized Ar uptake is plotted as a function of relative saturation pressure. Figure 2. Argon adsorption isotherms for microporous and nonmicroporous catalyst supports. The normalized Ar uptake is plotted as a function of relative saturation pressure.
Fig. 3.1. Evolution of the relative saturation (fi) for gibbsite toward equilibrium in an Oxisol. (Reprinted by permission of Oxford University Press from G. Sposito.12)... Fig. 3.1. Evolution of the relative saturation (fi) for gibbsite toward equilibrium in an Oxisol. (Reprinted by permission of Oxford University Press from G. Sposito.12)...
Calculate the relative saturation with respect to calcite and gypsum... [Pg.134]

Since the relative saturations are the same, owing to rapid equilibration between the various species, and hence the gradients are also equal, we can simplify and obtain... [Pg.42]


See other pages where Saturation relative is mentioned: [Pg.96]    [Pg.505]    [Pg.259]    [Pg.353]    [Pg.248]    [Pg.286]    [Pg.134]    [Pg.269]    [Pg.245]    [Pg.344]    [Pg.214]    [Pg.153]    [Pg.18]    [Pg.416]    [Pg.197]    [Pg.234]    [Pg.248]    [Pg.94]    [Pg.37]    [Pg.38]   
See also in sourсe #XX -- [ Pg.94 ]

See also in sourсe #XX -- [ Pg.253 ]

See also in sourсe #XX -- [ Pg.166 ]




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Relative permeability/saturation

Relative permeability/saturation relationships, wettability effects

Relative saturation , defined

Saturation Weight-Gain Levels Vs. Relative Humidity

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