KINETICS AND MECHANISM OF THE HETEROGENEOUS DECOMPOSITION OF NITRIC-OXIDE ON METAL-OXIDES IN THE PRESENCE OF HYDROCARBONS

Citation
Aj. Colussi et Vt. Amorebieta, KINETICS AND MECHANISM OF THE HETEROGENEOUS DECOMPOSITION OF NITRIC-OXIDE ON METAL-OXIDES IN THE PRESENCE OF HYDROCARBONS, The journal of physical chemistry. A, Molecules, spectroscopy, kinetics, environment, & general theory, 102(44), 1998, pp. 8486-8492
Citations number
39
Categorie Soggetti
Chemistry Physical
ISSN journal
10895639
Volume
102
Issue
44
Year of publication
1998
Pages
8486 - 8492
Database
ISI
SICI code
1089-5639(1998)102:44<8486:KAMOTH>2.0.ZU;2-Z
Abstract
Rates and products of the (3 + alpha)NO + CH4 --> 1/2(3 + alpha)N-2 (1 - alpha)CO + alpha CO2 + 2H(2)O (0 less than or equal to alpha less than or equal to 1) reaction were determined in low-pressure (NO/CH4/ O-2) mixtures ([NO] <1 mu M,[CH4] < 10[NO], [O-2] less than or equal t o [NO]; 1 mu M = 82 ppm at 1 atm, 1000 K) flowing over Sm2O3 between 1 000 and 1200 K. Samaria pretreated with CH4 (or N-2) at reaction tempe ratures instantly releases N-2 when exposed to NO. Prompt CO formation also occurs on methane-conditioned samples. In contrast, stationary o utflow gas compositions attain only after several reactor residence ti mes following step (NO + CH4) injections to the untreated catalyst. Ni tric oxide reduction rates R-No are roughly proportidnal to ([CH4] x [ NO])(1/2) but do not extrapolate to zero at [NO] - 0 and always increa se with T. We infer that: (1) there is no direct reaction between CH4 and NO on the catalyst surface; (2) instead, NO is reduced to N-2 by r eaction with oxygen vacancies V, and with nonvolatile carbon-containin g C-s species created in the heterogeneous oxidation/decomposition of CH4, respectively; (3) the entire mass, rather than just the surface, of catalyst microparticles participate in this phenomenon. We propose a purely heterogeneous mechanism in which physisorbed NO reacts with e ither vacancies in equilibrium with the active oxygen OR species respo nsible for CH4 oxidation or with C-s species. The derived kinetic law: R-(NO) = k(A)([NO](s)[CH4])(1/2) + (k(B)[CH4], with [NO](s) = [NO]/K- 8(-1) + [NO]), in conjunction with the reported Arrhenius parameters, closely fits rates measured under anoxic conditions. The fact that R-N O is unaffected by O-2 UP to F-O2 similar to 0.3F(NO) but drops at lar ger F-O2 inflows, even if O-2 is fully consumed in CH4 oxidation, is c onsistent with the competition of NO and Oz for vacancies. The dissimi lar observations made in experiments performed in the Torr range stron gly suggest that solid catalysts promote combustion at such relatively high pressures.