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    • 2. 发明专利
    • EXHAUST GAS DENITRATION METHOD
    • CA2260136C
    • 2003-07-08
    • CA2260136
    • 1997-07-10
    • MITSUBISHI HEAVY IND LTDOSAKA GAS CO LTD
    • NAKAMURA HITOSHIKOBAYASHI NORIHISASETOGUCHI TOSHIHIKOYASUTAKE AKINORIKASUH TAKAHIROYOSHIKAWA MASAAKIMOCHIDA ISAO
    • B01D53/56B01D53/54B01D53/86B01D53/94
    • This invention provides a process for the denitration of combustion exhaust gas which is suitable for use as a countermeasure while the exhaust gas has a low temperature (e.g., during the starting of combustion equipment) or for the denitration of a low-temperature portion of the exhaust gas. The aforesaid denitration process is a process for the denitration of combustion exhaust gas by passing the exhaust gas through an ammonia reduction denitrator, which comprises providing the exhaust gas flow path with a bypass having a low-temperature denitrator installed therein, on the downstream side of the ammonia reduction denitrator; while the exhaust gas has a low temperature, passing the exhaust gas through the bypass to perform the denitration thereof by means of the low-temperature denitrator; when the ammonia reduction denitrator has came to function properly, closing the bypass to perform the denitration of the exhaust gas by means of the ammonia reduction denitrator; and regenerating the catalyst within the low-temperature denitrator while the bypass is closed. In the aforesaid denitration process, a plurality of parallel-connected low-temperature denitrators may be installed in a section of the exhaust gas flow path where the exhaust gas temperature ranges from room temperature to 200.degree.C,and successively changed over in such a -23- way that denitration and catalyst regeneration are alternately performed. -24-
    • 5. 发明专利
    • DE69738296D1
    • 2007-12-27
    • DE69738296
    • 1997-07-10
    • MITSUBISHI HEAVY IND LTDOSAKA GAS CO LTD
    • MOCHIDA ISAOYASUTAKE AKINORISETOGUCHI TOSHIHIKOKOBAYASHI NORIHISANAKAMURA HITOSHIKASUH TAKAHIROYOSHIKAWA MASAAKI
    • B01D53/56B01D53/86B01D53/54B01D53/94
    • A method for denitration of combustion exhaust gas suitable for countermeasure for a low temperature exhaust gas produced at a start-up of a combustion device or for denitration of a low temperature part of the exhaust gas. The denitration method, in which denitration is performed by passing a combustion exhaust gas through an ammonia reduction denitration apparatus, comprises the steps of installing a bypass provided with a low temperature denitration apparatus and disposed on the downstream side of the ammonia reduction denitration apparatus in an exhaust gas flow passage, causing the low temperature denitration apparatus to perform denitration by passing the exhaust gas through the bypass when an exhaust gas temperature is low, causing the ammonia reduction denitration apparatus to perform denitration at a point of time when the ammonia reduction denitration apparatus comes to function fully, and regenerating a catalyst of the low temperature denitration apparatus while the bypass is closed. Further, the denitration method can perform denitration and regeneration of the catalyst by successively switching between low temperature denitration apparatuses of more than one systems which are installed in parallel in an area where a temperature of the exhaust gas in the exhaust gas flow passage ranges from room temperature to 200 DEG C.
    • 6. 发明专利
    • AT378101T
    • 2007-11-15
    • AT97930743
    • 1997-07-10
    • MITSUBISHI HEAVY IND LTDOSAKA GAS CO LTD
    • MOCHIDA ISAOYASUTAKE AKINORISETOGUCHI TOSHIHIKOKOBAYASHI NORIHISANAKAMURA HITOSHIKASUH TAKAHIROYOSHIKAWA MASAAKI
    • B01D53/56B01D53/86B01D53/54B01D53/94
    • A method for denitration of combustion exhaust gas suitable for countermeasure for a low temperature exhaust gas produced at a start-up of a combustion device or for denitration of a low temperature part of the exhaust gas. The denitration method, in which denitration is performed by passing a combustion exhaust gas through an ammonia reduction denitration apparatus, comprises the steps of installing a bypass provided with a low temperature denitration apparatus and disposed on the downstream side of the ammonia reduction denitration apparatus in an exhaust gas flow passage, causing the low temperature denitration apparatus to perform denitration by passing the exhaust gas through the bypass when an exhaust gas temperature is low, causing the ammonia reduction denitration apparatus to perform denitration at a point of time when the ammonia reduction denitration apparatus comes to function fully, and regenerating a catalyst of the low temperature denitration apparatus while the bypass is closed. Further, the denitration method can perform denitration and regeneration of the catalyst by successively switching between low temperature denitration apparatuses of more than one systems which are installed in parallel in an area where a temperature of the exhaust gas in the exhaust gas flow passage ranges from room temperature to 200 DEG C.
    • 7. 发明专利
    • EXHAUST GAS DENITRATION METHOD
    • CA2260136A1
    • 1998-01-22
    • CA2260136
    • 1997-07-10
    • MITSUBISHI HEAVY IND LTDOSAKA GAS CO LTD
    • KOBAYASHI NORIHISANAKAMURA HITOSHIKASUH TAKAHIROMOCHIDA ISAOYOSHIKAWA MASAAKISETOGUCHI TOSHIHIKOYASUTAKE AKINORI
    • B01D53/56B01D53/54B01D53/86B01D53/94
    • This invention provides a process for the denitration of combustion exhaust gas which is suitable for use as a countermeasure while the exhaust gas has a low temperature (e.g., during the starting of combustion equipment) or for the denitration of a low-temperature portion of the exhaust gas. The aforesaid denitration process is a process for the denitration of combustion exhaust gas by passing the exhaust gas through an ammonia reduction denitrator, which comprises providing the exhaust gas flow path with a bypass having a low-temperature denitrator installed therein, on the downstream side of the ammonia reduction denitrator; while the exhaust gas has a low temperature, passing the exhaust gas through the bypass to perform the denitration thereof by means of the low-temperature denitrator; when the ammonia reduction denitrator has came to function properly, closing the bypass to perform the denitration of the exhaust gas by means of the ammonia reduction denitrator; and regenerating the catalyst within the low-temperature denitrator while the bypass is closed. In the aforesaid denitration process, a plurality of parallel-connected low-temperature denitrators may be installed in a section of the exhaust gas flow path where the exhaust gas temperature ranges from room temperature to 200.degree.C,and successively changed over in such a -23- way that denitration and catalyst regeneration are alternately performed. -24-
    • 10. 发明专利
    • DE69738296T2
    • 2008-09-18
    • DE69738296
    • 1997-07-10
    • MITSUBISHI HEAVY IND LTDOSAKA GAS CO LTD
    • MOCHIDA ISAOYASUTAKE AKINORISETOGUCHI TOSHIHIKOKOBAYASHI NORIHISANAKAMURA HITOSHIKASUH TAKAHIROYOSHIKAWA MASAAKI
    • B01D53/56B01D53/86B01D53/54B01D53/94
    • A method for denitration of combustion exhaust gas suitable for countermeasure for a low temperature exhaust gas produced at a start-up of a combustion device or for denitration of a low temperature part of the exhaust gas. The denitration method, in which denitration is performed by passing a combustion exhaust gas through an ammonia reduction denitration apparatus, comprises the steps of installing a bypass provided with a low temperature denitration apparatus and disposed on the downstream side of the ammonia reduction denitration apparatus in an exhaust gas flow passage, causing the low temperature denitration apparatus to perform denitration by passing the exhaust gas through the bypass when an exhaust gas temperature is low, causing the ammonia reduction denitration apparatus to perform denitration at a point of time when the ammonia reduction denitration apparatus comes to function fully, and regenerating a catalyst of the low temperature denitration apparatus while the bypass is closed. Further, the denitration method can perform denitration and regeneration of the catalyst by successively switching between low temperature denitration apparatuses of more than one systems which are installed in parallel in an area where a temperature of the exhaust gas in the exhaust gas flow passage ranges from room temperature to 200 DEG C.