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Water vapour, equilibrium pressure

At equilibrium conditions, the rate at which water enters the bed with the feed Wu,f is equal fo fhe rafe af which it is removed at the condenser, W ,c- The gain in water vapour partial pressure in the fluidizing gas across the bed - p i) depends upon the volumetric flow rate of fluidizing gas Q, fhe fofal pressure in the system P, and the density of water vapour Thus... [Pg.208]

Fig. 3. Numerical simulation of unsteady rarefaction wave in mixture of nitrogen gas and water vapour A. pressure, B. temperature, C. vapour mass fraction, D. saturation ratio curves a frozen, f equilibrium b, c, d, e correspond to t/r = 10, 20, 40, 80, respectively Po = 1 bar. To = 295 K, fyo = 0.0136, ao = 350 m/s Xc = 2 piston velocity is 125 m/s. Fig. 3. Numerical simulation of unsteady rarefaction wave in mixture of nitrogen gas and water vapour A. pressure, B. temperature, C. vapour mass fraction, D. saturation ratio curves a frozen, f equilibrium b, c, d, e correspond to t/r = 10, 20, 40, 80, respectively Po = 1 bar. To = 295 K, fyo = 0.0136, ao = 350 m/s Xc = 2 piston velocity is 125 m/s.
Figure 4.42. Determination of RH for salt pairs. For the transformation (a), ASuniv at 15°C is calculated as a function of the partial pressure p of water vapour. Equilibrium corresponds to ASuniv being zero this condition is fulfilled for p 1129 Pa. Figure 4.42. Determination of RH for salt pairs. For the transformation (a), ASuniv at 15°C is calculated as a function of the partial pressure p of water vapour. Equilibrium corresponds to ASuniv being zero this condition is fulfilled for p 1129 Pa.
At this point the system has throe phases (CUSO4 CuS04,Hj0 HjO vapour) and the number of components is two (anhydrous salt water). Hence by the phase rule, F + F = C + 2, t.e., 3+F = 2 + 2, or F=l. The system is consequently univariant, in other words, only one variable, e.g., temperature, need be fixed to define the system completely the pressure of water vapour in equilibrium with CUSO4 and CuS04,Hj0 should be constant at constant temperature. [Pg.40]

We may now understand the nature of the change which occurs when an anhydrous salt, say copper sulphate, is shaken with a wet organic solvent, such as benzene, at about 25°. The water will first combine to form the monohydrate in accordance with equation (i), and, provided suflScient anhydrous copper sulphate is employed, the effective concentration of water in the solvent is reduced to a value equivalent to about 1 mm. of ordinary water vapour. The complete removal of water is impossible indeed, the equilibrium vapour pressures of the least hydrated tem may be taken as a rough measure of the relative efficiencies of such drying agents. If the water present is more than sufficient to convert the anhydrous copper sulphate into the monohydrate, then reaction (i) will be followed by reaction (ii), i.e., the trihydrate will be formed the water vapour then remaining will be equivalent to about 6 mm. of ordinary water vapour. Thus the monohydrate is far less effective than the anhydrous compound for the removal of water. [Pg.41]

Values of A for 20 C for other rare aases are Ne, O OIOI Kr, 0-0594 Xe. 0-126. S indicates the number of of gas measured at 0"C and 101 >325 kN which dissolve in 1 of water at the temperature staled, and when the pressure of the gas plus that of the water vapour is 101-325 kN m. A indicates the same quantity except that the gas itself is at the uniform pressure of 101-325 kN m when in equilibrium with water. [Pg.1345]

Example. — Ice and water-vapour are in equilibrium at + 0 0077° C., under a pressure of 4 57 mm., and liquid water is in equilibrium with water-vapour at the same temperature and pressure ice, liquid water, and water-vapour are therefore in equilibrium under these conditions, and the equilibrium curves representing pressures as functions of temperature meet at a triple point (0 0077° C., 4 57 mm.). These curves are (Fig. 47) ... [Pg.214]

The Smith—Topley (S—T) effect is the characteristic variation of isothermal dehydration rate (da /df)D with prevailing water vapour pressure (PHzo) shown in Fig. 10. (da/df)D first decreases with increasing PH2oi later rises to a maximum value and thereafter diminishes towards the zero rate of water loss that is achieved at the equilibrium dissociation pressure. For many hydrates, the reduction in (da/df)D from that characteristic of reaction in a good vacuum to that at PHzo 0.1 Torr is large (X 0.1) and the subsequent maximum may be more or less sharp. Since the reaction rate is, in general, represented by... [Pg.125]

The equilibrium relationships found by Sorrell (1977) were valid only for room temperature (22+2 °C) and, because samples were allowed to cure in sealed containers, for equilibrium water vapour pressures determined by the assembly of phases present. The phases which exist under such conditions were quite unequivocally found to be 4 1 5 and 1 1 2. However Sorrell pointed out that it is entirely possible that lower hydration states of either phase could be stable at higher temperatures or lower humidities. In particular the 4 1 4 phase (Feitknecht, 1933) may well be such a phase, particularly as one of the five waters of hydration is known to be held only loosely in the structure. Indeed, Sorrell reported that he observed a slight shoulder on the larger dehydration peak of the DTG curve of the 4 1 5 phase that might be assigned to the loss of this first water molecule. He did not, however, succeed in isolating or characterizing a 4 1 4 phase. [Pg.288]

At a given ambient water vapor pressure (usually the level found in the open atmosphere), the temperature of the material is raised so that the equilibrium water vapor pressure over the hydrated material is higher than the ambient water vapour pressure. Generally, heating up to 400 °C is sufficient to remove all the water of crystallization from materials. This removal of water yields a material which may contain some more strongly bound water. To remove this water, the material requires to be heated to a higher temperature (400-600 °C) so that the equilibrium water vapour pressure exceeds the ambient water vapour pressure. For near-complete removal of the last traces of water, temperatures as high as 1000 °C may be required. In addition to the heat required to raise the temperature of the material, heat is also required for the evaporation of water, which is an endothermic process. The enthalpy of evaporation increases as the water content, and hence the equilibrium water vapor pressure, decreases. [Pg.344]

The free volume density in water is fixed to the equilibrium value found for the water-vapour coexistence calculations [Pg.64]

Humidity of saturated air Mo. This is the humidity of air when it is saturated with water vapour. The air then is in equilibrium with water at the given temperature and pressure. [Pg.902]

Liquid absorbents. If the partial pressure of the water in the gas is greater than the equilibrium partial pressure at the surface of a liquid, condensation will take place as a result of contact between the gas and liquid. Thus, water vapour is frequently removed from a gas by bringing it into contact with concentrated sulphuric acid, phosphoric acid, or glycerol. Concentrated solutions of salts, such as calcium chloride, are also effective. The process may be carried out either in a packed column or in a spray chamber. Regeneration of the liquid is an essential part of the process, and this is usually effected by evaporation. [Pg.964]

Fig. 14. Change in ealcile saturation state during single-step adiabatic boiling (vapour saturation pressure) of aquifer water from four wet-steam wells in three areas Krafla. Iceland Momotnmho. Nicaragua and Zunil. Guatemala. A positive Sl-value corresponds to oversaluralion and a negative value to undersaturation. An SI of zero corresponds with equilibrium. SI is on a log Scale so an Sl-value of +1 indicates tenfold oversaturation. The numbers indicate well numbers. The calculated Sl-values for the aquifer waters (dots) depart a little from equilibrium. In view of all errors involved in the calculation of the Sl-values. the departure front equilibrium is. however, not significant. Nine that variations in Sl-values are more accurately calculated than absolute values. Fig. 14. Change in ealcile saturation state during single-step adiabatic boiling (vapour saturation pressure) of aquifer water from four wet-steam wells in three areas Krafla. Iceland Momotnmho. Nicaragua and Zunil. Guatemala. A positive Sl-value corresponds to oversaluralion and a negative value to undersaturation. An SI of zero corresponds with equilibrium. SI is on a log Scale so an Sl-value of +1 indicates tenfold oversaturation. The numbers indicate well numbers. The calculated Sl-values for the aquifer waters (dots) depart a little from equilibrium. In view of all errors involved in the calculation of the Sl-values. the departure front equilibrium is. however, not significant. Nine that variations in Sl-values are more accurately calculated than absolute values.
For a food system in equilibrium with a gaseous atmosphere (i.e. no net gain or loss of moisture to or from the system caused by differences in the vapour pressure of water), the equilibrium relative humidity (ERH) is related to aw by ... [Pg.221]

Sorption of water vapour to or from a food depends on the vapour pressure exerted by the water in the food. If this vapour pressure is lower than that of the atmosphere, absorption occurs until vapour pressure equilibrium is reached. Conversely, desorption of water vapour results if the vapour pressure exerted by water in the food is greater than that of the atmosphere. Adsorption is regarded as sorption of water at a physical interface between a solid and its environment. Absorption is regarded as a process in... [Pg.224]


See other pages where Water vapour, equilibrium pressure is mentioned: [Pg.267]    [Pg.370]    [Pg.16]    [Pg.270]    [Pg.344]    [Pg.239]    [Pg.407]    [Pg.94]    [Pg.117]    [Pg.195]    [Pg.49]    [Pg.393]    [Pg.80]    [Pg.386]    [Pg.21]    [Pg.22]    [Pg.37]    [Pg.343]    [Pg.657]    [Pg.117]    [Pg.213]    [Pg.151]    [Pg.51]    [Pg.43]    [Pg.366]    [Pg.99]    [Pg.12]    [Pg.217]    [Pg.132]    [Pg.132]   
See also in sourсe #XX -- [ Pg.271 ]




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