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Temperature conversion example

In the absence of a suitable soHd phase for deposition and in supersaturated solutions of pH values from 7 to 10, monosilicic acid polymerizes to form discrete particles. Electrostatic repulsion of the particles prevents aggregation if the concentration of electrolyte is below ca 0.2 N. The particle size that can be attained is dependent on the temperature. Particle size increases significantly with increasing temperature. For example, particles of 4—8 nm in diameter are obtained at 50—100°C, whereas particles of up to 150 nm in diameter are formed at 350°C in an autoclave. However, the size of the particles obtained in an autoclave is limited by the conversion of amorphous siUca to quartz at high temperatures. Particle size influences the stabiUty of the sol because particles <7 nm in diameter tend to grow spontaneously in storage, which may affect the sol properties. However, sols can be stabilized by the addition of sufficient alkaU (1,33). [Pg.489]

For example, the rate constant of the collinear reaction H -f- H2 has been calculated in the temperature interval 200-1000 K. The quantum correction factor, i.e., the ratio of the actual rate constant to that given by CLTST, has been found to reach 50 at T = 200 K. However, in the reactions that we regard as low-temperature ones, this factor may be as large as ten orders of magnitude (see introduction). That is why the present state of affairs in QTST, which is well suited for flnding quantum contributions to gas-phase rate constants, does not presently allow one to use it as a numerical tool to study complex low-temperature conversions, at least without further approximations such as the WKB one. ... [Pg.59]

These equations hold if an Ignition Curve test consists of measuring conversion (X) as the unique function of temperature (T). This is done by a series of short, steady-state experiments at various temperature levels. Since this is done in a tubular, isothermal reactor at very low concentration of pollutant, the first order kinetic applies. In this case, results should be listed as pairs of corresponding X and T values. (The first order approximation was not needed in the previous ethylene oxide example, because reaction rates were measured directly as the total function of temperature, whereas all other concentrations changed with the temperature.) The example is from Appendix A, in Berty (1997). In the Ignition Curve measurement a graph is made to plot the temperature needed for the conversion achieved. [Pg.105]

There are a number of 1,2-dihydroquinolines that are known to ring open when irradiated at low temperature. For example, irradiation of (74) at -196 °C in an EPA matrix results in the development of a pink color attributed to (75). Warming to room temperature causes reversion to (74). This cycle can be repeated several times with high conversions (72JCS(P2)17). The appropriate choice of substituents can result in transformations that have potential synthetic utility (equations 24 and 25) (69JA6513,73CC922). [Pg.371]

Conventional processes for preparing COCs have some common problems. The conversion of the cycloolefin may be low and further, a high amount of ethylene incorporated results in unsatisfactory low glass transition temperatures. Catalyst compositions have been developed in order to obtain materials with high glass transition temperatures (26). Examples are shown in Table 2.3. These catalysts are used for the copolymerization of ethene and norbornene. [Pg.47]

An aspect that has not received enough attention is the influence of pressure on the vitrification curve (Chapter 10). For some processes that operate at very high pressures there is a significant shift of the vitrification curve to lower temperatures for example, in the processing of phenolic molding compounds, where the polymerization may be arrested by vitrification at much lower temperatures than those predicted using Tg vs conversion values determined at ambient pressure. [Pg.266]

Figure 6.9 Temperature-conversion trajectory for a polytropic reactor for the substitution example reaction. The parameter is the switching temperature of the cooling system. Figure 6.9 Temperature-conversion trajectory for a polytropic reactor for the substitution example reaction. The parameter is the switching temperature of the cooling system.
The example represented in Figure 7.9 shows the extreme sensitivity of the temperature course towards the initial temperature. A change of only 1 °C from 103 to 104 °C results in a runaway. For too low temperatures, for example, 50 °C, a significant accumulation builds up. This results in a sudden acceleration of the reaction (ignition), but the conversion is only 0.95 after 10 hours. Thus, the different states presented in Section 5.2.3.5, that is, runaway above 100°C, marginal ignition below 60 °C, and QFS (Quick on-set, Fair conversion and Smooth profile) between 70 and 90 °C are represented [10]. [Pg.164]

Furthermore, it is necessary to ensure that after sample taking, the reaction is being quenched immediately. This is usually not a big problem for reactions at higher temperatures, for example, the oxidative conversion of hydrocarbons. However, for reactions carried out in the liquid phase near room temperature or at only slightly elevated temperatures, this might very well be a problem. [Pg.261]

Chloropurines are less reactive and the displacement with cyanide under these conditions was unsuccessful. However, the use of tetraethylammonium cyanide with trimethylamine as catalyst allows this conversion to be carried out very readily at room temperature an example is the formation of 7. ... [Pg.520]

Note These conversion factors refer to temperature intervals, not temperatures For example, to find the number ot Celsius degrees between 32 F and 212°F you can say that... [Pg.62]


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Temperature conversions

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