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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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OP-I-14T(K)17001600150014001300120011001000Low temp linear PM (LTLPM)Q, cal/ mole1001010,10,011E-329-32The same as above"208-25900(LTLPM)+2 recomb. CH 3O 20,0 0,1 0,2 0,3 0,4 0,5 0,6 0,70,00 0,05 0,10 0,15time, s0,551E-4time, sWhile, <strong>the</strong> maxima <strong>of</strong> both heat release and temperature prove to be much greater just in<strong>the</strong> case <strong>of</strong> <strong>the</strong> initial reaction rate slowing down with <strong>the</strong> quadratic reactions (at right), one <strong>of</strong>which is highly exo<strong>the</strong>rmic. The last, apparently, is one <strong>of</strong> stronger preheating sources in <strong>the</strong>reaction zone. Thus, in this case <strong>the</strong> system got more energy for an initiating <strong>of</strong> following heatabsorption stage, being be trigger <strong>of</strong> all possible endo<strong>the</strong>rmic processes. Then, <strong>the</strong> graduallyweakening brunched oxygen cycle competes with equally hardening oxygen-free one, and <strong>the</strong>second rising stage begins. Judging by <strong>the</strong> reactions which contribute to heat release on thisstage, <strong>the</strong> H atoms and СН 3 radicals, released from <strong>the</strong> peroxide form, play a leading part init, while <strong>the</strong> role <strong>of</strong> oxidizer comes to water. Thus, if one will be extended at now <strong>the</strong>responsible variant <strong>of</strong> model by observable number <strong>of</strong> reactions <strong>of</strong> <strong>the</strong>se active agents and<strong>the</strong>ir interactions product, <strong>the</strong>n it has be reached a good level <strong>of</strong> <strong>the</strong> description <strong>of</strong> <strong>the</strong> mixedchain-heat process <strong>of</strong> combustion oneself. The kinetic features <strong>of</strong> <strong>the</strong> system are analyzedresponsible for <strong>the</strong> influence <strong>of</strong> different factors on <strong>the</strong> process regimes.The work is supported under project No.6025 on <strong>the</strong> RAS Presidium Program <strong>of</strong>physical-chemical investigations «New Approaches to <strong>the</strong> Fuels Chemistry and PowerEngineering».References1. Griffits, S.F. / Progress Energy Combustion Sci. / 1995. 21: 25-107.2. Peterson, E.L., S.F. Davidson, and R.K. Hanson. / Combustion Flame. / 1999.117: 272-90.3. Lam, S.H. / Comb. Sci. & Technology / 1993. 89: 375-404.4. Ivanova A.N., Tarnopolskii B.L., and Karnaukh A.A. / Kinetics and <strong>Catalysis</strong>. / 1997.38. (4).485-494.5. Karnaukh A.A, and Ivanova A.N. / Kinetics and <strong>Catalysis</strong>. / 2005. 46 (1), 10-20.6. Karnaukh A.A, and Ivanova A. // Proceedings <strong>of</strong> Semenov Memorial at 2003-Biennale «Combustion andAtmospheric Pollution» (St. Petersburg). // Edited by: Roy G.D., Frolov S.M., and Starik A.M. Moscow,TORUS_PRESS, 2003, P. 67-72.7. Kostenko S.S., Polianczyk E.V., Karnaukh A.A., Ivanova A.N., and Manelis G.B. / Chem. Phys. Reports(Rus). 2006. V.25. No.5, 53-63.8. Kostenko S.S., Polianczyk E.V., Karnaukh A.A, Ivanova A.N., and Manelis G.B.// Proceedings <strong>of</strong> NEPCAPBiennale -2005 (Sochi).// Edited by: Roy G.D., Frolov S.M., and Starik A.M. Moscow, TORUS-PRESS,2005, P-223-22953

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