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Temperature and water vapor pressure, 152

The extent of dealumination was found (166) to be limited by the degree of ammonium exchange of the starting material, and also to depend on the temperature and water vapor pressure during treatment. Depending on the conditions, any desired composition of the product up to Si/Al 8 could be... [Pg.267]

Figure 13.13 A schematic illustration of the membrane distillation process showing temperature and water vapor pressure gradients that drive the process... Figure 13.13 A schematic illustration of the membrane distillation process showing temperature and water vapor pressure gradients that drive the process...
On the basis of above results, the activation energy can be calculated, and the theoretical values of the crack growth rate under various temperatures and water vapor pressures can be evaluated. Because the crack velocity at a given stress intensity factor is proportional to water vapor pressure, Eq.( 1) becomes ... [Pg.532]

Figure 5. The distribution of the crack velocity under various temperature and water vapor pressure. Figure 5. The distribution of the crack velocity under various temperature and water vapor pressure.
Substituting the values of and vo into Eq.(9), the theoretical values of the crack velocity can be calculated. In Figure 5, the distribution of the theoretical crack velocity at Ki = K, under various temperature and water vapor pressure is shown. The relation between the observed values, v" , and the theoretical values, v, of the crack velocity at Kf = K, is shown in Figure 6, where the straight line indicates the line of v = v . It can be shown that the theoretical crack velocity agrees well with the observed crack velocity. Therefore, It can be made sure that the crack velocity at a given stress intensity factor under various water vapor pressure can be estimated. [Pg.533]

Capacitive sensors are employed to measure the dew point temperature of gas in the flow chamber. Accurate empirical correlations exist between dew point temperatures and water vapor pressures. If the characteristic diffusion time for water in the gas is short compared to both the turnover time of gas in the flow chamber and the characteristic timescale for water transport through the bulk membrane, then the water vapor pressure of the outlet stream, equals the average vapor pressure in the flow chamber, P". [Pg.373]

In this case, n -r = 2 (water and calcium sulfate) and therefore v = 2. The water content of the solution is a function of temperature and water vapor pressure above the sohd (see section 3.7.3). [Pg.73]

Although other techniques can be used to measure the relative humidity above a saturated solution, one relatively simple procedure is to utilize a vacuum system to remove air from the headspace (by vapor phase expansions) and then, with the vacuum pumps isolated and the saturated solution maintained at a constant temperature, measure water vapor pressure. Water vapor pressure can... [Pg.396]

At sea level, Pj is approximately 1 atm, but exhibits some temporal and spatial variability. For example, the annual mean pressure in the northern hemisphere is 0.969 atm and in the southern hemisphere is 0.974 atm, with monthly averages varying by as much as 0.0001 atm, i.e., about 1 mbar (1 atm = 1013.25 mbar). These fluctuations are caused by spatial and temporal variations in atmospheric temperature and water vapor content associated with weather, and seasonal and longer-term climate shifts. Pj is also affected by diurnal atmospheric tides, and it decreases with increasing altitude above sea level. Some gases, such CO2 and O2, exhibit seasonal variability that is caused in part by seasonal variability in plant and animal activity (see Figures 25.4 and 6.7). [Pg.150]

Fig. Z58 Biocompatible solvents (Acetone, ethanol and water) vapor pressure and temperature... Fig. Z58 Biocompatible solvents (Acetone, ethanol and water) vapor pressure and temperature...
A remarkable uniformity has been found to exist in the behavior of all gases under changing conditions. Three simple statements, the so-called gas laws, suffice to define with a considerable degree of accuracy the volume changes with changing pressure, temperature, and water-vapor content. [Pg.41]

The aim of the AirLight Experiment is to verify the relation of the fluorescence photon production to the ionization energy deposit, Eq. (2), and to measure the fluorescence yield y A, T, p) of electrons in air around their minimum ionizing energy between 500 keV and 2 MeV. The fluorescence yield will be studied in several wavelength bands for different air pressures, temperatures and water vapor contaminations. [Pg.405]

The reaction probability 7 depends in general on the physical nature and chemical composition of the particle and on temperature. The composition of the liquid or solid particles is derived from thermodynamic considerations. The value of 7 for different conditions is determined in the laboratory. In the case of liquid sulfuric acid aerosols, for most reactions, 7 depends on the weight percentage W (wt%) of H2SO4 in the aerosol. W can be expressed as a function of temperature T(K) and water vapor pressure Ph2o (hPa) by (Steele and Hamill, 1981 Hanson et al, 1994)... [Pg.35]

EXAMPLE 15 (fl) A mixture of oxygen and water vapor at a total pressure of 107 kPa is in equilibrium with liquid water at 25°C, at which temperature the water vapor pressure is 3.2 kPa. Calculate the pressure of the oxygen, (b) Oxygen is collected over water at 25°C under a barometric pressure of 107 kPa. (PH2O = 3.2 kPa) Calculate the pressure of the oxygen. [Pg.95]

Several obvious advantages exist in measuring gas tension. First, pressure can be measured very accurately with highly stable pressure sensors. Second, measurements of O2 and gas tension allow an estimate of the partial pressure of N2 to be made. This estimate is based on the fact that under conditions typical of natural waters, O2, N2 and water vapor comprise more than 99% of the gas tension signal. Thus, subtraction of the O2 partial pressure and water vapor pressure (practically, a function of temperature and salinity) from gas tension provides very nearly the partial pressure of N2, a gas that is considered almost inert in the oceans. [Pg.70]

We changed the ammonia concentration and water vapor pressure and measured the ammonia sensor s output under various combinations of the two. The sensor reading response took several seconds because responses took time even if water vapor pressure was varied while keeping ammonia concentration at zero. We attributed this response time to the responsiveness of the system as a whole. The sensor s output was tested in ambient temperature, which varies with time. The response time curve of sensor has been observed at different concentration. Our ammonia sensor is quite capable of detecting even low ammonia concentrations of about 0.01 ppm. [Pg.59]

Figure 3. Droplet temperature and mass variation with time. Solid lines represent Runge-Kutta approximations based on energy-material balance for droplet with initial temperature of Tq = 5°C exposed to flowing air at = 25°C and water vapor pressure = 2.5 times that for water at 5 C. Points are experimentally obtained values. Figure 3. Droplet temperature and mass variation with time. Solid lines represent Runge-Kutta approximations based on energy-material balance for droplet with initial temperature of Tq = 5°C exposed to flowing air at = 25°C and water vapor pressure = 2.5 times that for water at 5 C. Points are experimentally obtained values.
Acetylene burns in air with an intensely hot, luminous, and smoky flame. The ignition temperatures of acetylene and of acetylene-air and acetylene-oxygen mixtures vary according to composition, initial pressure, initial temperature, and water vapor content. As a typical example, an air mixture containing 30 percent acetylene by volume at atmospheric pressure can be ignited at about 581 °F (305°C). The flammable limits of acetylene-air and acetylene-oxygen mixtures similarly depend on initial pressure, temperature, and water vapor content. In air at atmospheric pressure, the upper flammable limit is about 80 percent acetylene by volume and the lower limit is 2.5 percent acetylene. Some references list the upper flammable limit as 100 percent, which is due to the de-... [Pg.214]


See other pages where Temperature and water vapor pressure, 152 is mentioned: [Pg.494]    [Pg.285]    [Pg.723]    [Pg.192]    [Pg.403]    [Pg.274]    [Pg.247]    [Pg.494]    [Pg.285]    [Pg.723]    [Pg.192]    [Pg.403]    [Pg.274]    [Pg.247]    [Pg.343]    [Pg.384]    [Pg.214]    [Pg.528]    [Pg.384]    [Pg.112]    [Pg.59]    [Pg.223]    [Pg.496]    [Pg.110]    [Pg.113]    [Pg.17]    [Pg.161]    [Pg.366]    [Pg.7]    [Pg.667]    [Pg.265]    [Pg.226]    [Pg.417]    [Pg.397]    [Pg.271]    [Pg.182]    [Pg.1507]   


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