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Atmospheric data temperature

The critical data for sulphur trioxide have been found to be as follows 2 Critical pressure, 83-8 atmospheres critical temperature, 218-3° C. critical density, 0-633. [Pg.141]

Studies of sintering and redispersion of supported metal catalysts have been reviewed by several authors [M8] most of these reviews focus on early kinetic studies of sintering of supported metal catalysts using a simplified power law expression (SPLE). Unfortunately this crude approach does not permit sintering kinetics to be presented in a consistent way nor does it enable (1) useful extrapolation of the data to other conditions (2) useful quantitative comparisons between different studies, or (3) physically meaningful kinetic parameters to be obtained. The ultimate result has been confusion regarding the effects of reaction parameters such as atmosphere and temperature and of catalyst properties such as support promoters, etc., on sintering rates. [Pg.2]

Figure 8.3. Contact angles of liquid Sn on (100) plane of diamond versus temperature in an Ar-10% H2 atmosphere. Data from work reported in (Nogi et al. 1998) [7]. Figure 8.3. Contact angles of liquid Sn on (100) plane of diamond versus temperature in an Ar-10% H2 atmosphere. Data from work reported in (Nogi et al. 1998) [7].
The tropospheric sulfur chemistry is different. Unlike the nitrogen and carbon chemistry, where combustion is an insignificant source, the combustion source of SO2 appears to be very important. While OH reactions can be shown to convert sulfides to SO2, it is not clear that normal atmospheric chemistry is important in the next step—the conversion of S02 to H2SO, which is then removed from the atmosphere by rainout. It has also been suggested that a large amount of SO2 is removed directly by rainout. Unfortunately we have the fewest data, both kinetic and atmospheric, on sulfur compounds. Most of the kinetic data we do have are at high temperatures, and most of the atmospheric data are for polluted environments. [Pg.504]

The high pressure adsorption of single gases and mixtures can be predicted from the low pressure (sub-atmospheric) data for the same systems. The optimum temperature for measuring the aulsorption of single gases is near their critical temperature where both the Henry s constant auid the absolute saturation capacity can be determined accurately. [Pg.49]

A pressurized direct-drive concentric cylinder viscometer system (Figure 3-21) was used to obtain shear rate versus shear stress data on a tomato puree at several fixed temperatures between 76 and 120°C (Figure 3-22), and temperature versus apparent viscosity data at several shear rates on a 4% waxy rice (WR) starch dispersion during gelatinization over the temperature range 30 to 110°C (Figure 3-23) (Rao et al., 1998). The drive motor, torque unit, and concentric cylinder unit and temperature control vessel of a Haake RV2 viscometer system (Haake Inc.) were placed in a chamber (PRC) that could be pressurized to 0.2 MPa (two atmospheres). The temperature control vessel was insulated to minimize heat loss. A eopper-constantan (36 gage wires) thermocouple plaeed in the well of the inner eoneentric eylinder measured the temperature of the test sample. [Pg.89]

In this paper, the effect of sintering atmosphere and temperature on the activity of a typical three-way autoinotive exhaust catalyst system (Pt/Rh/y-Al O /CeO ) and the implications of correlating fundamental catalyst characterization data such as average noble metal crystallite size and composition with catalytic activity are discussed. [Pg.539]

From tlie results of their work on the effect of pressure on ignition temperature, Tausz and Schulte concluded that the effect was so variable that no predictions could be made from atmospheric data as to what the temperatures would be under pressure.000 This uncertainty is due largely to the influence of other complicating factors, such as the effect of pressure... [Pg.327]

The solubility of CO in water, expressed as mole fraction of CO in the liquid phase, is given for pressures up to atmospheric and temperatures of 0 to 100 °C. Note that 1 standard atmosphere equals 101.325 kPa. The references give data over a wider range of temperature and pressure. The estimated uncertainty is about 2%. [Pg.1279]

Most kinetic data regarding the thermal conversion of coal are known for relatively low temperatures (< 1200 K) and heating rates (< 10" K/s), which will be discussed in this section. Kinetic pecuharities related to higher temperatures and higher coal heating rates are less available and will be considered in Section 10.4.7. Heating of coal in an inert atmosphere to temperatures of 620-670 K leads to its decomposition with the formation of primary volatile destraction products and coke. Formation and release of the volatile... [Pg.708]

NMR measurements have been combined with elemental and mass balance data to determine the extent of aromatization during pyrolysis. Hershkowitz et al7 were the first to quantify the increase in the aromatic carbon formed during pyrolysis of Colorado oil shale. Their experiments were conducted at a slow heating rate, under high pressure (2600 kPa) N2 or H2 atmospheres, at temperatures up to 600°C, followed by a 10 min soak period at this temperature. In an N2 atmosphere, the total aromatic carbon in the products increased by 83% over that in the raw shale. In H2 the increase was only 17%. In addition, 87% of the raw shale carbon was recovered in the oil when heated under H2, compared with 67% under N2. An increase in aromatic carbon of about 83% has been observed in pyrolysis studies of Green River oil shale at heating rates of l-720 Ch to 500°C. ... [Pg.231]

Although the activities have been determined under differing reaction temperatures, they have been extrapolated to 300°C and 350°C as a means of comparison. The data in the tables illustrates a number of features of the reaction. Comparison has been made between the conditions of pretreatment, such as vacuum versus oxygen atmospheres. The temperature of the vacuum pre-treatment was carefully controlled, as previous studies had shown that when the sample was pre-heated too high in vacuum, a... [Pg.120]

To calculate the masses of the liquids injected it is necessary to know the densities of the liquids at the temperature and pressure in the injectors. The injectors are not thermostatted but set above the bath in an air-conditioned room. Because the injectors themselves have a large heat capacity, rapid fluctuations in the room temperature will not have a major effect. Long-term drifts in the temperature would be more serious. Compression of the liquids to 500 kPa will cause an increase in density of about 0.05 per cent. Van Ness points out that there will be a negligible error in the mole fraction calculated from atmospheric data provided all volume measurements on both liquids are made at the same applied pressure and the liquids have similar isothermal compressibilities. When the isothermal compressibilities of the two components differ appreciably a more detailed calculation is necessary to determine the mole fraction. [Pg.19]

A number of polymer films and fibers have been examined as a function of temperature. Dynamic measurements were made at 11 Hz, l C/min heating rate in nitrogen atmosphere. Data point of dynamic tensile modulus and tan 6 were obtained at 1°C increments. This is essentially a continuous monitoring of the changes in storage modulus, loss modulus, and tan 6 and length of sample. [Pg.88]


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Temperature data

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