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Practice of Kinetics (Comprehensive Chemical Kinetics, Volume 1)

Practice of Kinetics (Comprehensive Chemical Kinetics, Volume 1)

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30 EXPERIMENTAL METHODS FOR SLOW REACTIONS3.2.3 Comparison <strong>of</strong> flow and static systemsIn a static system, a finite time is required for the reactant or reactants to fillthe RV and acquire the RV temperature. This renders initial pressure determination(by graphical extrapolation) and initial rate measurements somewhat suspect.(Heating may be assisted by having a heated dosing or mixing vessel.) In practice,filling and heating take 5-15 sec, depending on the conditions, and have to be verymuch faster than the rate <strong>of</strong> the reaction studied. This limits the study <strong>of</strong> thedecomposition <strong>of</strong> dtBP, for example, to a maximum temperature <strong>of</strong> 160-170" C.Leads to and from the RV and pressure-measuring devices contribute to the production<strong>of</strong> a "dead space". Ideally, this dead space should amount to no morethan 4 % <strong>of</strong> the RV volume. Corrections for dead space have to be made withpressure measurements and subsequent kinetic expressions' 03. However, for lowextents <strong>of</strong> reaction no (or very simple) corrections are necessary. For adiabaticreactions in large diameter RV's, errors in rate coefficient values may be significant',due to the production <strong>of</strong> thermal gradients. Very <strong>of</strong>ten, for a partly heterogeneousreaction, it is difficult to isolate or to determine the rate <strong>of</strong> the homogeneous process2.Flow systems, with low contact times, have the advantage that higher temperaturesmay be used, thus minimising or obviating heterogeneous processes. Also,percentage conversion may be kept low, while still retaining precision in determiningthe extent <strong>of</strong> reaction, since a run can last until sufficient product has accumulated,thus minimising any further reactions <strong>of</strong> the initial products. The inherenterrors associated with rate coefficients determined using conventional flow system~''~have led to relatively little use <strong>of</strong> this technique in spite <strong>of</strong> its advantages.However, the use <strong>of</strong> a stirred flow RV obviates most <strong>of</strong> these difficultie~~~ andtogether with a static system allows a reaction to be studied over a wide pressureand large temperature range. Two difficulties remain. In spite <strong>of</strong> heat exchangethe heat capacity effect <strong>of</strong> the gases entering the RV lowers the temperature <strong>of</strong> theRV centre relative to the walls9', and instantaneous cooling still does not occurupon leaving the reaction zone. Thermal gradients will also still be present dueto the endothermicity or exothermicity <strong>of</strong> a reaction. Low pressures should beused to minimise the heat capacity effect. However, the use <strong>of</strong> low pressures maylead to pressure-dependent rate coefficients"5 and therefore make bond dissociationenergies, determined for example by the toluene carrier gas technique'06,suspect. Also, side reactions may not be insignificant'". Conversely, the flowsystem is ideal for the study <strong>of</strong> pressure-dependent decompositions or isomerisations<strong>of</strong> free radicals, whose rate coefficients are close to their high pressure limitsat normal pressures with static systems, At the higher temperatures used in theflow system, the transition pressure from second to first order kinetics for a unimolecularreaction will also occur at a higher pressure'.t The transition pressure varies as the (s-3)th power <strong>of</strong> the absolute temperature, where sis the number <strong>of</strong> oscillators contributing to the decomposition (see ref. 108).

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