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Humidity chart for

Fig. 3. Humidity chart for the ait—water system, molal quantities. To convert kj to Btu, divide by 1.054 to convert cm to fT, multiply by 35.31 X 10 ... Fig. 3. Humidity chart for the ait—water system, molal quantities. To convert kj to Btu, divide by 1.054 to convert cm to fT, multiply by 35.31 X 10 ...
FIG. 12-4 Humidity chart for air-water vapor mixtures. To convert British thermal units per pound to joules per Idlo-gram, multiply by 2326 to convert British thermal units per pound dry air-degree Fahrenheit to joules per Idlogram-kelvin, multiply hy 4186.8 and to convert cubic feet per pound to cubic meters per kilogram, multiply by 0.0624. [Pg.1155]

Humidity charts for other solvent vapors may be prepared in an analogous manner. There is one important difference involved, however, in that the wet-bulb temperature differs considerably from the adiabatic-saturation temperatures for vapors other than water. [Pg.1177]

Figures 12-37 to 12-39 show humidity charts for carbon tetrachloride, oenzene, and toluene. The lines on these charts have been calculated in the manner outlined for air-water vapor except for the wet-bulb-temperature lines. The determination of these hnes depends on data for the psychrometric ratio /j Z/c, as indicated by Eq. (12-22). For the charts shown, the wet-bulb-temperature hnes are based on the following equation ... Figures 12-37 to 12-39 show humidity charts for carbon tetrachloride, oenzene, and toluene. The lines on these charts have been calculated in the manner outlined for air-water vapor except for the wet-bulb-temperature lines. The determination of these hnes depends on data for the psychrometric ratio /j Z/c, as indicated by Eq. (12-22). For the charts shown, the wet-bulb-temperature hnes are based on the following equation ...
FIGURE 23.1 Humidity chart for mixtures of air and water (pressure of 101.325 kPa). [Pg.1672]

HUMIDITY CHARTS FOR SYSTEMS OTHER THAN AIR-WATER. A humidity chart may be constructed for any system at any desired total pressure. The data required are the vapor pressure and latent heat of vaporization of the condensable component as a function of temperature, the specific heats of pure gas and vapor, and the molecular weights of both components. If a chart on a mole basis is desired, all equations can easily be modified to the use of molal units. If a chart at a pressure other than 1 atm is wanted, obvious modificatioi in the above equations may be made. Charts for several common systems besides air-water have been published. ... [Pg.746]

Figure 9.3-2. Humidity chart for mixtures of air and water vapor at a total pressure of 101.325 kPa 760 mm Hg). (From R. E. Treybal, Mass-Transfer Operations, 3rd ed. New York McGraw-Hill Book Company, 1980. With permission.)... Figure 9.3-2. Humidity chart for mixtures of air and water vapor at a total pressure of 101.325 kPa 760 mm Hg). (From R. E. Treybal, Mass-Transfer Operations, 3rd ed. New York McGraw-Hill Book Company, 1980. With permission.)...
The enthalpy of saturated air is plotted versus 7] on an // versus T plot as shown in Fig. 10.5-3. This enthalpy is calculated with Eq. (9.3-8) using the saturation humidity from the humidity chart for a given temperature, with 0°C (273 K) as a base temperature. Calculated values are tabulated in Table 10.5-1. [Pg.606]


See other pages where Humidity chart for is mentioned: [Pg.1149]    [Pg.1177]    [Pg.972]    [Pg.1000]    [Pg.764]    [Pg.1153]    [Pg.1181]    [Pg.550]    [Pg.195]   
See also in sourсe #XX -- [ Pg.528 ]




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