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Fall-off-plots

According to Eq. (1.7), the fall-off plot depends not only on the value of the unimolecular rate constant, /cj, but also on the collisional activation, fc, and deactivation, k.1, rate constants. The bimolecular reactions both complicate and aid the analy-... [Pg.5]

Until about 1960, fall-off plots were the major source of quantitative information about unimolecular reactions. In order to adapt the microcanonical RRKM theory to these thermal data, it was necessary to take into account the internal energy of the reactants by rewriting Eqs. (1.4)-(1.6) as follows ... [Pg.9]

Fig. 1. A schematic fall-off plot for a unimolecular rate constant as function of pressure. Fig. 1. A schematic fall-off plot for a unimolecular rate constant as function of pressure.
As initially proposed by Rice and further described by Bunker and Hase, an intrinsic non-RRKM molecule should have at least one false high-pressure limit in its unimolecular fall-off plot of k versus pressure. The true unimolecular rate constant is observed as p -> CO where p is the pressure. The rate constants at the false high-pressure limit or limits are related to the transition rates between vibrational states. Thus, it should be possible to detect intrinsic non-RRKM behavior by measuring k i over the complete pressure range. However, there are several difficulties associated with this procedure. It is very difficult to perform unimolecular experiments at high pressure, and, as recently noted by Thiele et unimole-... [Pg.19]

The operating characteristics of a pump are conveniently shown by plotting the head h, power P, and efficiency r> against the flow Q as shown in Figure 8.24. It is important to note that the efficiency reaches a maximum and then falls, whilst the head at first falls slowly with Q but eventually falls off rapidly. The optimum conditions for operation are shown as the duty point, i.e. the point where the head curve cuts the ordinate through the point of maximum efficiency. [Pg.335]

In an experimental study of a small air-lift pump(6), (25 mm. diameter and 13.8 m overall height) the results were expressed by plotting the efficiency of the pump, defined as the useful work done on the water divided by the energy required for isothermal compression of the air, to a basis of energy input in the air. In each case, the curve was found to rise sharply to a maximum and then to fall off more gradually. Typical results are shown in Figure 8.37. [Pg.363]

The drag reduction experiments show that the characteristics of drag reduction are the same as Habon-G solution reported earlier The amount of drag reduction stays almost the same for the first several hours. Then the amount of drag reduction falls off to zero abruptly as shown in Fig. 1. In the figure we plot the % friction reduction against sheared time, where the % friction reduction, % FR, is defined as follows ... [Pg.690]

The following criteria are usually applied when analyzing these power spectra the magnitude of power, the frequency at which the power begins to fall off, and the slope of the descending part of the plot. From such an analysis one can sufficiently well identify the various types of corrosive attack (uniform, crevice, pitting). [Pg.628]

Nonlinear Arrhenius Plots For most organic reactions, plots of In k versus l/T are linear, and afford and A values in accord with the Arrhenius equation." However, for systems where QMT is involved, rate constants fall off less steeply than expected as temperatures are lowered, which often leads to upwardly curved Arrhenius plots as illustrated in Figure 10.2 ... [Pg.420]

The points for Ag and Pd-Ag alloys lie on the same straight line, a compensation effect, but the pure Pd point lies above the Pd-Ag line. In fact, the point for pure Pd lies on the line for Pd-Rh alloys, whereas the other pure metal in this series, i.e., rhodium is anomalous, falling well below the Pd-Rh line. Examination of the many compensation effect plots given in Bond s Catalysis by Metals (155) shows that often one or other of the pure metals in a series of catalysts consisting of two metals and their alloys falls off the plot. Examples include CO oxidation and formic acid decomposition over Pd-Au catalysts, parahydrogen conversion (Pt-Cu) and the hydrogenation of acetylene (Cu-Ni, Co-Ni), ethylene (Pt-Cu), and benzene (Cu-Ni). In some cases, where alloy catalysts containing only a small addition of the second component have been studied, then such catalysts are also found to be anomalous, like the pure metal which they approximate in composition. [Pg.174]

No catalyst has an infinite lifetime. The accepted view of a catalytic cycle is that it proceeds via a series of reactive species, be they transient transition state type structures or relatively more stable intermediates. Reaction of such intermediates with either excess ligand or substrate can give rise to very stable complexes that are kinetically incompetent of sustaining catalysis. The textbook example of this is triphenylphosphine modified rhodium hydroformylation, where a plot of activity versus ligand metal ratio shows the classical volcano plot whereby activity reaches a peak at a certain ratio but then falls off rapidly in the presence of excess phosphine, see Figure... [Pg.6]

Figure 7-6 are plotted in Figure 7-7. The absorbed energy falls off more rapidly with latitude than does the long-wave flux. Transport in this climate system carries excess energy away from the tropics to higher latitudes where there is a deficit in the energy budget. Figure 7-6 are plotted in Figure 7-7. The absorbed energy falls off more rapidly with latitude than does the long-wave flux. Transport in this climate system carries excess energy away from the tropics to higher latitudes where there is a deficit in the energy budget.
The graph shows that the peak amount of E is reached in about 200 days. The plot of F falls off only slightly beyond t = 1000. [Pg.306]

The results are presented as plots of DP against mole fraction of isobutene. With methyl chloride, methylene dichloride, or vinyl chloride as diluent the DP rises very steeply to a sharp peak with increasing monomer concentration, and then falls off in a curve of exponential type (Figure 4). With ethyl chloride there is apparently no maximum, the... [Pg.68]

The intensity of the fluorescence emission detected at the photodetector stage was plotted as a function of temperature over the same range, and this is shown in Figure 11.22. It falls off rapidly with temperature increase over the whole temperature region. This does not contradict the experimental evidence of Burns and Nathan(56) who showed that the fluorescence quantum efficiency of the ruby fluorescence integrated over the entire band from 620 to 770 nm is independent of temperature (to 5%) in the region from-196 to 240°C, for the emission detected here is only the A-line part of the total fluorescence emission. [Pg.360]

In spite of the proper qualitative features of the Lindemann-Hinshelwood model, it does not correctly predict the much broader experimental fall-off behavior this is shown in Fig. 18, in which log(fe/fc ,) is plotted as a function of log(M = P/RT/Mj = Pc/RT). As evident from this figure, the actual rate at the center of fall-off (i.e., at PJ is depressed relative to the L-H model consequently, the transition of rate from low- to high-pressure limit occurs more gradually. [Pg.164]

In the preceding expression, log(FJ is related to the depression of the fall-off curve at the center relative to the L-H expression in a og k/k ) vs. log(2f/(l -I- X)) plot. The values for F<. can then be related to the properties of specific species and reaction and temperature using methods discussed in Gardiner and Troe (1984). In Fig. 19, values of F for a variety of hydrocarbon decompositions are presented. As evident from this figure, in the limit of zero or infinite temperatures and pressures, all reactions exhibit Lindemann-Hinshelwood behavior and F approaches unity. From this figure, it is clear that L-H analysis generally does an adequate job in... [Pg.165]

Figure 3-17 Plot of eqdlibrimn convereion Xg vasus terr5)er-ature for ammonia synthesis starting with stoichiomeh ic feed. While the equilibrium is favorable at anbient tar5)erature (where bactaia fix N2), the convasion r dly falls off at elevated temperature, and commercial ammonia synthesis reactors operate with a Fe catalyst at pressiues as high as 300 atm to att 2 high equilibrium conversion. Figure 3-17 Plot of eqdlibrimn convereion Xg vasus terr5)er-ature for ammonia synthesis starting with stoichiomeh ic feed. While the equilibrium is favorable at anbient tar5)erature (where bactaia fix N2), the convasion r dly falls off at elevated temperature, and commercial ammonia synthesis reactors operate with a Fe catalyst at pressiues as high as 300 atm to att 2 high equilibrium conversion.
Here rh is the hydrated radius or Stokes radius of the protein. On this assumption s will be expected to increase with the relative molecular mass approximately as Mr2/3. A plot of log s against log Mr should be a straight line. Figure 3-8 shows such a plot for a number of proteins. The plots for nucleic acids, which can often be approximated as rods rather than spheres, fall on a different line from those of proteins. Furthermore, the sedimentation constant falls off more rapidly with increasing molecular mass than it should for spheres. [Pg.109]

Relationships between Tb and Nc or M in homologous series are nonlinear. The difference in Tb between successive members of n-alkanes is not constant. It falls off continuously, demonstrated by plotting Tb against Nc (C1-C40) [5]. The following equation has been reported for n-alkanes (C6-C18) [6,7] ... [Pg.95]


See other pages where Fall-off-plots is mentioned: [Pg.5]    [Pg.103]    [Pg.5]    [Pg.103]    [Pg.99]    [Pg.262]    [Pg.234]    [Pg.99]    [Pg.89]    [Pg.366]    [Pg.42]    [Pg.94]    [Pg.574]    [Pg.253]    [Pg.233]    [Pg.67]    [Pg.47]    [Pg.134]    [Pg.16]    [Pg.466]    [Pg.214]    [Pg.749]    [Pg.58]    [Pg.500]    [Pg.110]    [Pg.84]    [Pg.145]    [Pg.616]    [Pg.24]    [Pg.1503]    [Pg.1504]   
See also in sourсe #XX -- [ Pg.5 , Pg.6 , Pg.9 ]




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