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Selective catalytic reduction catalyst modules

To illustrate the validity of the models presented in the previous section, results of validation experiments using lab-scale BSR modules are taken from Ref. 7. For those experiments, the selective catalytic reduction (SCR) of nitric oxide with excess ammonia served as the test reaction, using a BSR filled with strings of a commercial deNO catalyst shaped as hollow extrudates (particle diameter 1.6 or 3.2 mm). The lab-scale BSR modules had square cross sections of 35 or 70 mm. The kinetics of the model reaction had been studied separately in a recycle reactor. All parameters in the BSR models were based on theory or independent experiments on pressure drop, mass transfer, or kinetics none of the models was later fitted to the validation experiments. The PDFs of the various models were solved using a finite-difference method, with centered differencing discretization in the lateral direction and backward differencing in the axial direction the ODEs were solved mostly with a Runge-Kutta method [16]. The numerical error of the solutions was... [Pg.385]

Another interesting research in the area of catalysis is developing catalytic processes which could be controlled by external switches. Organometallic complexes capable of reversible processes are the first candidate for this purpose. Oxidation-reduction is one of these reversible processes which could be extensively modulating reactivity and selectivity of the catalyst through the redox control of the supporting ligand in a metal complex. [Pg.249]


See other pages where Selective catalytic reduction catalyst modules is mentioned: [Pg.188]    [Pg.270]    [Pg.263]    [Pg.413]    [Pg.49]    [Pg.390]    [Pg.390]    [Pg.139]    [Pg.495]    [Pg.341]    [Pg.130]   
See also in sourсe #XX -- [ Pg.337 , Pg.338 ]




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