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Activation eneigy

The Arrhenius relationship (eq. 5) for crystalline polymers or other transitions, where Ea is the activation eneigy and R the gas constant (8.3 J/mol), is as follows ... [Pg.151]

The unsaturation present at the end of the polyether chain acts as a chain terminator in the polyurethane reaction and reduces some of the desired physical properties. Much work has been done in industry to reduce unsaturation while continuing to use the same reactors and holding down the cost. In a study (102) using 18-crown-6 ether with potassium hydroxide to polymerize PO, a rate enhancement of approximately 10 was found at 110°C and slightly higher at lower temperature. The activation eneigy for this process was found to be 65 kj/mol (mol ratio, r = 1.5 crown ether/KOH) compared to 78 kj/mol for the KOH-catalyzed polymerization of PO. It was also feasible to prepare a PPO with Mn 10,000 having narrow distribution at 40°C with added crown ether (r = 1.5) (103). The polymerization rate under these conditions is about the same as that without crown ether at 80°C. [Pg.352]

In considering the physical forces acting in fission, use may be made of the Bohr liquid drop model of the nucleus. Here it is assumed that in its uonual energy state, a nucleus is spherical and lias a homogeneously distributed electrical charge. Under the influence of the activation eneigy furnished by the incident nentron, however, oscillations are set up which tend to deform the nucleus. In the ellipsoid form, the distribution of the protons is such that they are concentrated in the areas of the two foci. The electrostatic forces of repulsion between the protons at the opposite ends of the ellipse may then further deform the nucleus into a dumbbell shape. Rrom this condition, there can be no recovery, and fission results. [Pg.201]

For true first-order bond rupture reactions, the activation eneigy, E, is equal to the eneigy of the ruptured bond, and following the transition-state theory (35), the pre-exponential factor, kro> is... [Pg.56]

The overall requirement is 1.0—2.0 s for low eneigy waste compared to typical design standards of 2.0 s for RCRA hazardous waste units. The most important, ie, rate limiting steps are droplet evaporation and chemical reaction. The calculated time requirements for these steps are only approximations and subject to error. For example, formation of a skin on the evaporating droplet may inhibit evaporation compared to the theory, whereas secondary atomization may accelerate it. Errors in estimates of the activation eneigy can significandy alter the chemical reaction rate constant, and the pre-exponential factor from equation 36 is only approximate. Also, interactions with free-radical species may accelerate the rate of chemical reaction over that estimated solely as a result of thermal excitation therefore, measurements of the time requirements are desirable. [Pg.56]

The classical experiment tracks the off-gas composition as a function of temperature at fixed residence time and oxidant level. Treating feed disappearance as first order, the pre-exponential factor (kr and activation eneigy, E, in the Arrhenius expression (eq. 35) can be obtained. These studies tend to confirm large activation energies typical of the bond rupture mechanism assumed earlier. However, an accelerating effect of the oxidant is also evident in some results, so that the thermal rupture mechanism probably overestimates the time requirement by as much as several orders of magnitude (39). Measurements at several levels of oxidant concentration are useful for determining how important it is to maintain spatial uniformity of oxidant concentration in the incinerator. [Pg.57]

Computer Models. The actual residence time for waste destruction can be quite different from the superficial value calculated by dividing the chamber volume by the volumetric flow rate. The large activation eneigies for chemical reaction, and the sensitivity of reaction rates to oxidant concentration, mean that the presence of cold spots or oxidant deficient zones render such subvolumes ineffective. Poor flow patterns, ie, dead zones and bypassing, can also contribute to loss of effective volume. The tools of computational fluid dynamics (qv) are useful in assessing the extent to which the actual profiles of velocity, temperature, and oxidant concentration deviate from the ideal (40). [Pg.57]

Activation Parameters. Thermal processes are commonly used to break labile initiator bonds in order to form radicals. The amount of thermal eneigy necessary varies with the environment, but absolute temperature, T> is usually the dominant factor. The energy barrier, the minimum amount of eneigy that must be supplied, is called the activation eneigy, E. A third important factor, known as the frequency factor, 4, is a measure of bond motion freedom (translational, rotational, and vibrational) in the activated complex or transition state. The relationships of Af E and T to the initiator decomposition rate (kJ) are expressed by the Arrhenius first-order rate equation (eq. 16) where R is the gas constant, and jA and Ea are known as the activation parameters. [Pg.221]

Subsequently, Frejacques [29] and Cottreh, Graham and Reid [30] continued the experiments within die ranges of 310-440°C mid 380-430°C, wider 4-40 mm and 200-400 mm pressures respectively. They confirmed the previous statement that the reaction is of the first order, with activation eneigies of 42.8 mid 53.6 kcal/mole respectively. The reaction constant, k, may be calculated, according to Cottrell et al, from the equation... [Pg.582]

Oxidation, All inorganic siUcon hydrides are readily oxidized. Silane and disilane are pyrophoric in air and form siUcon dioxide and water as combustion products thus, the soot from these materials is white. The activation eneigies of the reaction of silane with molecular and atomic oxygen have been reported (20,21). The oxidation reaction of dichlorosilane under low pressure has been used for the vapor deposition of siUcon dioxide (22). [Pg.22]

Fig. 23. Representative protecting groups for phenolic and carboxjdic acid-based systems, (a) The polymer-based protecting groups are listed in order of increasing activation eneigy for acid-catalyzed deprotection, (b) Acid-labile monomeric dissolution inhibitors, a bifunctional system based on protected bisphenol A. (c) Another system that combines the function of dissolution inhibitor and PAG in a single unit. Fig. 23. Representative protecting groups for phenolic and carboxjdic acid-based systems, (a) The polymer-based protecting groups are listed in order of increasing activation eneigy for acid-catalyzed deprotection, (b) Acid-labile monomeric dissolution inhibitors, a bifunctional system based on protected bisphenol A. (c) Another system that combines the function of dissolution inhibitor and PAG in a single unit.
The activation eneigy, also called the energy barrier for a... [Pg.113]

This temperature dependence reveals that the activation eneigy (EJ for layer and framework silicate weathering reactions is high (>12 kilocalories or 50 kilojoules/ mole), evidence that the dissolution process is not diffusion controlled, but is limited by a slow surface reaction such as the protonation of a surface group or the rupture of a metal-oxygen bond. [Pg.226]


See other pages where Activation eneigy is mentioned: [Pg.104]    [Pg.303]    [Pg.207]    [Pg.266]    [Pg.308]    [Pg.496]    [Pg.122]    [Pg.504]    [Pg.540]    [Pg.365]    [Pg.766]    [Pg.566]    [Pg.337]    [Pg.352]    [Pg.445]    [Pg.457]    [Pg.52]    [Pg.56]    [Pg.149]    [Pg.221]    [Pg.515]    [Pg.505]    [Pg.8]    [Pg.483]    [Pg.149]    [Pg.81]    [Pg.258]    [Pg.47]    [Pg.50]    [Pg.1001]    [Pg.126]    [Pg.455]    [Pg.893]    [Pg.157]    [Pg.131]   
See also in sourсe #XX -- [ Pg.153 , Pg.155 ]




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