1995
DOI: 10.1016/0920-5861(95)00156-8
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Development of a high-temperature combustion catalyst system and prototype catalytic combustor turbine test results

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Cited by 29 publications
(3 citation statements)
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“…Hence, essentially little, if any, catalytic activity may be exhibited by several of the channels while a majority of the channels may, on an individual basis, provide quite satisfactory performance. Because of this, the material passing through the channels having less catalytic activity may not undergo the catalytic reaction or at least not to the extent experienced by other portions of the reactants [23,24]. Further, when honeycomb catalysts are employed in exothermic catalytic reactions, they are subjected to excessive temperatures, often in excess of 1600 K to 2000 K or more, which can lead to deactivation of the catalytically-active components thereon and even adversely affect the skeletal support.…”
Section: Introductionmentioning
confidence: 99%
“…Hence, essentially little, if any, catalytic activity may be exhibited by several of the channels while a majority of the channels may, on an individual basis, provide quite satisfactory performance. Because of this, the material passing through the channels having less catalytic activity may not undergo the catalytic reaction or at least not to the extent experienced by other portions of the reactants [23,24]. Further, when honeycomb catalysts are employed in exothermic catalytic reactions, they are subjected to excessive temperatures, often in excess of 1600 K to 2000 K or more, which can lead to deactivation of the catalytically-active components thereon and even adversely affect the skeletal support.…”
Section: Introductionmentioning
confidence: 99%
“…High activity is favored by a high catalyst surface area (Arai et al, 1986;Zwinkels et al, 1995). The activity and stability requirements are usually in conflict (McCarty and Wise, 1990), and hence engineering solutions have been proposed to circumvent the contradiction between activity and stability, such as a hybrid combustor (Furuya et al, 1987), a partial catalytic combustor (Dalla Betta et al, 1994), and a multimonolith combustor (Sadamori et al, 1994). The first two combustor concepts limit the catalyst temperature by converting only part of the fuel over the catalyst and the remainder in a homogeneous downstream combustion zone.…”
Section: Introductionmentioning
confidence: 99%
“…1. Design goals of the catalytic combustor were proposed by one of authors as shown in Table 1 (Sadamori et al, 1994). The concept of the combustor is that the combustion occurs within the honeycomb-shaped combustion catalyst layer.…”
Section: Model Description (Experimental Apparatus)mentioning
confidence: 99%