Handbook of Heterogeneous Catalysis 2008
DOI: 10.1002/9783527610044.hetcat0124
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Catalytic Combustion

Abstract: The sections in this article are Introduction Base Concepts and System Requirements Design Approaches Fully Catalytic Combustor Fuel Staging Partial Catalytic Hybrid Combustor Commercialization Status and Perspectives Fuel‐Rich Catalyti… Show more

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Cited by 4 publications
(4 citation statements)
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“…In this context, besides choosing a material that is inert at the operating pressure and temperature and can act synergistically with the active component, selecting a support facilitates modularization. Industry requires high flow rates, short contact times, tight temperature control, and low pressure drop across the bed . Pressure drops across structured catalysts are 2 orders of magnitude lower than those across packed beds, and radial and axial temperature gradients (local hot spots) are lower due to the higher effective thermal conductivity and the regularity of the internal path, which makes it possible to operate in the laminar regime …”
Section: Introductionmentioning
confidence: 99%
“…In this context, besides choosing a material that is inert at the operating pressure and temperature and can act synergistically with the active component, selecting a support facilitates modularization. Industry requires high flow rates, short contact times, tight temperature control, and low pressure drop across the bed . Pressure drops across structured catalysts are 2 orders of magnitude lower than those across packed beds, and radial and axial temperature gradients (local hot spots) are lower due to the higher effective thermal conductivity and the regularity of the internal path, which makes it possible to operate in the laminar regime …”
Section: Introductionmentioning
confidence: 99%
“…Character of the axial dependences of Nu predicted by the model using the 3-D Navier−Stokes equations is rather typical (see, for instance, the available results 7,8,11 ). For the conditions under study the Nusselt number is much higher in the inlet domain, and then some smooth lowering is observed.…”
Section: Industrial and Engineering Chemistry Researchmentioning
confidence: 97%
“…The profiles of gas velocity magnitude and "radial" (transverse) component of the gas velocity (Figure 6) as well as methane fraction in the reaction mixture (Figure 8) are presented vs transversal Y-coordinate (0 < Y < 0.69 mm, Z = 0) at the cross sections along the catalyst length, mainly according to the 2-D pictures shown in Figure 5. Lines 1−8 in Figures 6 and 8 correspond to the next axial coordinates X = 0 (1), 0.1 (2), 0.2 (3), 0.5 (4), 1 (5), 5 (6), 10 (7), and 29 mm (8). The temperature profiles along the monolith length are shown in Figure 7.…”
Section: Systemmentioning
confidence: 99%
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