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公开(公告)号：EP2087547B1
公开(公告)日：2014-10-15
申请号：EP07824400.1
申请日：2007-10-31
发明人： DEVRIENDT, James , MORGAN, Robert , BARNARD, Paul , LEAH, Robert
CPC分类号： H01M8/0662 , H01M8/04014 , H01M8/04029 , H01M8/04067 , H01M8/04156 , H01M8/0618 , H01M2008/1293 , H01M2250/20 , Y02E60/36 , Y02E60/525 , Y02T90/32
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公开(公告)号：EP2364512B1
公开(公告)日：2016-01-06
申请号：EP09760965.5
申请日：2009-11-26
CPC分类号： F24H9/2007 , F24D12/02 , F24D2200/04 , F24D2200/19 , F24H1/0036 , F24H1/08 , F24H1/22 , F24H9/06 , F24H9/14 , F24H9/148 , F24H2240/00 , F24H2240/04 , F24H2240/10 , F24H2240/12 , H01M2250/405 , Y02B10/70 , Y02B30/14 , Y02B90/16 , Y02E20/14 , Y02T10/166
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公开(公告)号：EP2364512A2
公开(公告)日：2011-09-14
申请号：EP09760965.5
申请日：2009-11-26
CPC分类号： F24H9/2007 , F24D12/02 , F24D2200/04 , F24D2200/19 , F24H1/0036 , F24H1/08 , F24H1/22 , F24H9/06 , F24H9/14 , F24H9/148 , F24H2240/00 , F24H2240/04 , F24H2240/10 , F24H2240/12 , H01M2250/405 , Y02B10/70 , Y02B30/14 , Y02B90/16 , Y02E20/14 , Y02T10/166
摘要： A boiler unit (100) housed in an enclosure, the boiler unit (100) configured to receive a solid state combined heat and power generating device (130). The boiler unit (100) comprises a heating device (110) to produce heat; and a control unit (120) to independently control each of the heating device (110) and the solid state combined heat and power generating device (130). The boiler unit (100) is operable without the solid state combined heat and power generating device (130) being present.
摘要翻译： 锅炉单元（100），其容纳在外壳中，所述锅炉单元（100）被配置为接收固态组合式热和发电装置（130）。 锅炉单元（100）包括产生热量的加热装置（110） 以及独立地控制所述加热装置（110）和所述固态组合式发热装置（130）中的每一个的控制单元（120）。 锅炉单元（100）可操作，而不存在固态组合式发热装置（130）。
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公开(公告)号：EP2044644B1
公开(公告)日：2012-11-07
申请号：EP07733427.4
申请日：2007-06-29
CPC分类号： H01M8/04302 , H01M8/04022 , H01M8/04037 , H01M8/04223 , H01M8/04303 , H01M8/0618 , H01M8/0631 , H01M2008/1293
摘要： Methods of reforming hydrocarbon fuel for supply at staff-up to a fuel cell stack comprising at least one solid oxide fuel cell, during transient load increases and during shutdown using a steam reformer (SR), alone initially run as partial oxidation reformer (CPOX) at start-up (or preferably with a separate CPOX) to heat cell and SR to operating temperature whereupon CPOX is shut down; the CPOX is started up to provide extra fuel rapidly for the fuel cell stack when the latter suffers increased load; and at shutdown the reforming is switched to CPOX to allow inert/blanket gas containing mostly nitrogen to be supplied to the cell stack whilst it cools enough to allow air entry. The CPOX may be supplied with water/steam to permit some autothermal reforming.
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公开(公告)号：EP2087547A1
公开(公告)日：2009-08-12
申请号：EP07824400.1
申请日：2007-10-31
发明人： DEVRIENDT, James , MORGAN, Robert , BARNARD, Paul , LEAH, Robert
CPC分类号： H01M8/0662 , H01M8/04014 , H01M8/04029 , H01M8/04067 , H01M8/04156 , H01M8/0618 , H01M2008/1293 , H01M2250/20 , Y02E60/36 , Y02E60/525 , Y02T90/32
摘要： A system and method are provided for exchanging heat in fuel cell systems (100) in which the anode and cathode off-gases are provided with separated flow paths. In one embodiment, where a fuel cell stack (110) has separate anode and cathode off-gas flow paths, separate anode off-gas from the at least one fuel cell stack (110) and at least one heat transfer fluid are passed through a first heat exchange element (126) to exchange heat between the anode off-gas and the heat transfer fluid. The cathode off-gas exiting the at least one fuel cell stack is then combined with the anode off-gas from the heat exchange element (126) in a burner and burned.
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公开(公告)号：EP2044644A2
公开(公告)日：2009-04-08
申请号：EP07733427.4
申请日：2007-06-29
CPC分类号： H01M8/04302 , H01M8/04022 , H01M8/04037 , H01M8/04223 , H01M8/04303 , H01M8/0618 , H01M8/0631 , H01M2008/1293
摘要： Methods of reforming hydrocarbon fuel for supply at staff-up to a fuel cell stack comprising at least one solid oxide fuel cell, during transient load increases and during shutdown using a steam reformer (SR), alone initially run as partial oxidation reformer (CPOX) at start-up (or preferably with a separate CPOX) to heat cell and SR to operating temperature whereupon CPOX is shut down; the CPOX is started up to provide extra fuel rapidly for the fuel cell stack when the latter suffers increased load; and at shutdown the reforming is switched to CPOX to allow inert/blanket gas containing mostly nitrogen to be supplied to the cell stack whilst it cools enough to allow air entry. The CPOX may be supplied with water/steam to permit some autothermal reforming.
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