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Channel parallel reaction

Montanari el al., for example, studied a Co—H-MFI sample through FT-IR spectroscopy of in situ adsorption and coadsorption of probe molecules [o-toluonitrile (oTN), CO and NO] and CH4-SCR process tests under IR operando conditions. The oTN adsorption and the oTN and NO coadsorption showed that both Co2+ and Co3+ species are present on the catalyst surface. Co3+ species are located inside the zeolitic channels while Co2+ ions are distributed both at the external and at the internal surfaces. The operando study showed the activity of Co3+ sites in the reaction. The existence of three parallel reactions, CH4-SCR, CH4 total oxidation and NO to NOz oxidation, was also confirmed. Isocyanate species and nitrate-like species appear to be intermediates of CH4-SCR and NO oxidation, respectively. A mechanism for CH4-SCR has been proposed. On the contrary, Co2+ substitutional sites, very evident and predominant in the catalyst, which are very hardly reducible, seemed not to play a key role in the SCR process [173],... [Pg.128]

In the absence of a long-lived intermediate, the time constants for product formation must be the same for the two branches of the parallel reactions giving triplet products or singlet products each appearance time is given by the reciprocal of the sum of the rates for the two parallel channels. As discussed above the appearance time for the production of the singlet... [Pg.316]

The present work deals with the study of the liquid phase phenol alkylation by (-butanol over the three types of catalysts derived from MWW-precursor MCM-22, MCM-36 and ITQ-2. It was assumed that by pillaring and/or delamination the contribution of acid sites located on the hemicages will increase and it could be evidenced during the alkylation of phenol by (-butanol, process involving large reaction intermediates and products which are difficult to be accommodated within sinusoidal channels. The reaction pathway involves many parallel and/or successive steps, the main reactions being O-alkylation and C-alkylation. The catalytic activity and selectivity of these materials are discussed. A general scheme of the process is proposed on the basis of the structural and acidic features of the catalysts. [Pg.357]

M 39] [P 37] The Reynolds-stress model describes best the experimental findings out of three turbulent models investigated (see Figure 1.105) [41]. Then, the model was used for predictions of the mixing efficiency as determined by an azo-type parallel reaction. It was found that the wall thickness has no major influence, whereas the channel depth, as expected, has an influence, affecting the shearing. [Pg.136]

Direct asymmetric cpl-induced photoreactions are only observed if there are two enantiomeric ground state reactants presgntthat absorb different amounts of light. Thus the asymmetry of the cpl source is transformed into a different concentration of excited-state enantiomeric species, which becomes obvious in emitting systems in the circular polarization of luminescence [7]. These in turn react in a nonchiral environment with the same rate constants for the different deactivation channels. Thus asymmetric photoreactions are dependent or independent parallel reactions of the enantiomers with different net rates. [Pg.5]

Direct competition between parallel reaction channels should be explicitly considered in the systems where multiple dissociation channels exist. Again, CRUNCH includes this capability. [Pg.248]

Most of the generated reactions were eliminated during the construction of the mechanism. The primary tool was the comparison of reaction rates for parallel reaction channels. This approach required careful planning of the order of generation of the reaction types. The program was used for the pyrolysis of C1-C4 hydrocarbons. Mechanisms for ethane, propane and butane contained 15, 49 and 76 species and 18, 115 and 179 reactions, respectively. These mechanisms were compared with schemes which had been proposed by human experts. Most of the reactions were identical, and, in general, the program proposed a superset of those presented in the literature. [Pg.306]

The reaction between amidogen and hydroxyl radicals was found to be a key reaction in the modeling of thermal De-NOx reaction kinetics.8 However, there were no direct measurements of the kinetics of the reaction NH2 + OH until the experiments performed by Fagerstrom et al.22s The following parallel reaction channels were taken into account in describing the reaction kinetics... [Pg.208]

The chapter is organized as follows. In the remainder of the introduction the investigated molecular systems are introduced. The experimental section describes a typical pump-probe setup for experiments with a very high time resolution. Then the transient absorption and the contributing processes are discussed. In the fourth section a model of the reaction mechanism is developed from the experimental findings. Then we discuss briefly the situation of parallel reaction channels, and finally the results and conclusion are summarized. [Pg.350]

The heart of the system is a microreactor packaging scheme that is based upon a commercially available microchip socket. This approach allows the silicon-based reactor die, which contains dual parallel reaction channels with more than 100 electrical contacts, to be installed and removed in a straightforward fashion without removing any fluidic and electronic connections. Various supporting microreactor functions, such as gas feed flow control, gas feed mixing, and various temperature control systems, are mounted on standard CompactPCI electronic boards. The boards are subsequently installed in a commercially available computer chassis. Electrical connections between the boards are achieved through a standard backplane and custom-built input-output PC boards. A National Instruments embedded real-time processor is used to provide closed-loop process control and... [Pg.363]

Catalysts not only accelerate a chemical reaction, but also help to channel a reaction to produce a desired product. This selectivity does not contradict the fact that the position of equilibrium itself cannot be influenced. It only means that under given circumstances, one of the many possible spontaneous parallel reactions will be considerably more accelerated than the others. For example, the process of hydrogenating carbon monoxide (Fischer-Tropsch synthesis) can produce methanol (catalysts ZnO, Cr203) or unsaturated hydrocarbons (catalyst Fe), depending upon the type of catalyst used and the reaction conditions. In contrast, we use the term specificity if a catalyst only affects certain substances. Very high selectivity and specificity can be found in reactions catalyzed by enzymes. These are very important reactions that will be gone into more detail in the next section. [Pg.460]

ROSS - Only in the case of parallel reactions, that is more than one product channel for a given set of reactants then external periodic perturbations can enhance the yield of one channel over the other. [Pg.458]

Microreaction system with 32 parallel reaction channels... [Pg.53]

The use of MRs, particularly catalytic wall microreactors, for the SR of methane/NG allows supply of the heat necessary to drive the endothermic reaction by the catalytic oxidation of methane or any other fuel in a series of channels parallel to those in which reforming occurs [192]. Parametric analysis of the thermal behaviour suggests that whatever the nature of the catalyst used in the exothermic channels, the strongest influence comes from the activation energies of both exothermic and endothermic reactions [192]. Unbalancing heat consumed... [Pg.112]


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See also in sourсe #XX -- [ Pg.418 ]




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