IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0155397
(2008-06-03)
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등록번호 |
US-8122719
(2012-02-28)
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발명자
/ 주소 |
- Griffin, Timothy
- Winkler, Dieter
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출원인 / 주소 |
|
대리인 / 주소 |
Buchanan Ingersoll & Rooney PC
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인용정보 |
피인용 횟수 :
0 인용 특허 :
11 |
초록
▼
Apparatus for combustion of a fuel-oxidizer mixture in a combustion chamber of a turbogroup, in particular of a power plant wherein total oxidizer flow is divided into a main oxidizer flow and a secondary oxidizer flow. The main oxidizer flow is lean mixed with a main fuel flow in a premix burner, a
Apparatus for combustion of a fuel-oxidizer mixture in a combustion chamber of a turbogroup, in particular of a power plant wherein total oxidizer flow is divided into a main oxidizer flow and a secondary oxidizer flow. The main oxidizer flow is lean mixed with a main fuel flow in a premix burner, and the mixture is fully oxidized in the combustion chamber. The secondary oxidizer flow is divided into a pilot oxidizer flow and a heat-exchanging oxidizer flow. The pilot oxidizer flow is rich mixed with a pilot fuel flow, and the mixture is partially oxidized in a catalyst, with hydrogen being formed. Downstream of the catalyst, the partially oxidized pilot fuel-oxidizer mixture and the heat-exchanging oxidizer flow are together introduced into at least one zone which is suitable for stabilizing the combustion of the main fuel-oxidizer mixture.
대표청구항
▼
1. An apparatus for the combustion of a fuel-oxidizer mixture in a combustion chamber of a turbogroup, in particular a power plant, comprising: a premix burner, in which, when the apparatus is operating, a main oxidizer flow is lean mixed with a main fuel flow and this main fuel-oxidizer mixture is
1. An apparatus for the combustion of a fuel-oxidizer mixture in a combustion chamber of a turbogroup, in particular a power plant, comprising: a premix burner, in which, when the apparatus is operating, a main oxidizer flow is lean mixed with a main fuel flow and this main fuel-oxidizer mixture is fully oxidized;at least one catalyst, which is designed, when the apparatus is operating, to partially oxidize a rich pilot fuel-oxidizer mixture flowing through it so as to form hydrogen, the at least one catalyst including a heat exchanger;an oxidizer supply device which, when the apparatus is operating, admixes a heat-exchanging oxidizer flow to the partially oxidized pilot fuel-oxidizer mixture downstream of the catalyst, the heat-exchanging oxidizer flow exchanges heat with the rich pilot fuel-oxidizer mixture, in the heat exchanger;wherein the catalyst and the oxidizer supply device being designed in such a way that, when the apparatus is operating, they introduce the partially oxidized pilot fuel-oxidizer mixture and the heat-exchanging oxidizer flow together into at least one zone that is suitable for stabilizing the combustion of the main fuel-oxidizer mixture. 2. The apparatus as claimed in claim 1, wherein the catalyst has a catalytically active path through which medium can flow and a catalytically inactive path through which medium can flow in parallel with the catalytically active path,the catalytically active path is designed to partially oxidize a rich pilot fuel oxidizer mixture flowing through it, with hydrogen being formed, in that the catalytically inactive path is coupled to the catalytically active path in such a manner as to exchange heat, forms part of the oxidizer supply device and has the heat-exchanging oxidizer flow flowing through it when the apparatus is operating. 3. The apparatus as claimed in claim 2, wherein the catalyst has a plurality of channels, through which medium can flow in parallel and of which some are catalytically active and the others are catalytically inactive, in that the catalytically active path of the catalyst is formed by its catalytically active channels, in that the catalytically inactive path of the catalyst is formed by its catalytically inactive channels. 4. The apparatus as claimed in claim 3, wherein a pilot fuel pipe is connected to the catalytically active channels, in such a manner that, when the apparatus is operating, it introduces the pilot fuel flow separately into the individual catalytically active channels. 5. The apparatus as claimed in claim 2, wherein a pilot oxidizer pipe is connected to the catalytically active path,a pilot fuel pipe is connected to the pilot oxidizer pipe upstream of the catalyst. 6. The apparatus as claimed in claim 1, wherein the catalyst is arranged concentrically in a head of the premix burner. 7. The apparatus as claimed claim 1, wherein the catalyst is arranged in a lance which is arranged concentrically in a head of the premix burner and projects into the premix burner. 8. The apparatus as claimed claim 1, wherein a distribution head is positioned upstream of the catalyst, a first entrance of which the distribution head is connected to a pilot fuel-oxidizer mixture pipe, a second entrance of which the distribution head is connected to a heat-exchanging oxidizer pipe and an exit of which the distribution head is connected to the catalyst,the distribution head has a plurality of shafts which are adjacent transversely with respect to the direction of flow and are all open at the exit and are selectively open at the first entrance or at the second entrance. 9. The apparatus as claimed in claim 3, wherein the catalytically active channels and the catalytically inactive channels are distributed in such a way that first lines of catalytically active channels arranged next to one another and second lines of catalytically inactive channels arranged next to one another are arranged alternately with one another, in particular in alternate lines,first shafts, which are open toward the first entrance, adjoin the first lines and second shafts, which are open toward the second entrance, adjoin the second lines. 10. The apparatus as claimed in claim 9, wherein a plate with holes, of which the hole pattern is selected in such a way that each channel is in communication with one of the shafts through a single through hole, is arranged between the distribution head and the catalyst. 11. The apparatus as claimed in claim 10, wherein the catalytically active channels and the catalytically inactive channels are arranged alternately in a chessboard pattern,the hole pattern of the plate with holes and the arrangement of the channels are adapted to one another in such a way that the catalytically active channels are in communication with the first shafts, which lead to the first entrance of the distribution head, via the associated through holes, whereas the catalytically inactive channels are in communication with the second shafts, which lead to the second entrance of the distribution head, via the associated through holes.
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