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1.
公开(公告)号:EP4434622A1
公开(公告)日:2024-09-25
申请号:EP22892328.0
申请日:2022-06-16
发明人: WATANABE, Nobufumi
摘要: Provided are a method of regenerating a nitrous oxide-decomposing catalyst such that a deactivated nitrous oxide-decomposing catalyst can be efficiently regenerated, and a method of decomposing nitrous oxide while using a nitrous oxide-decomposing catalyst regenerated by the regeneration method.
Disclosed are:
a method of regenerating a nitrous oxide-decomposing catalyst, which includes the step of heat-treating a nitrous oxide-decomposing catalyst under a condition in an oxidizing gas atmosphere at a temperature of 175 to 325°C, in which the nitrous oxide-decomposing catalyst includes a titanium oxide-containing carrier carrying a component containing at least one kind selected from the group consisting of ruthenium and ruthenium compounds, and has been used for a nitrous oxide-decomposing reaction; and
a method of decomposing nitrous oxide, which includes the step of bringing the nitrous oxide-decomposing catalyst regenerated by the regeneration method into contact with a nitrous oxide-containing gas containing nitrous oxide.-
公开(公告)号:EP4403247A1
公开(公告)日:2024-07-24
申请号:EP22883585.6
申请日:2022-10-18
发明人: SUGIURA, Takuya , TSUJIUCHI, Tatsuya , TANAKA, Hiroshi , HIRATA, Takuya , IMADA, Junji , SHINDO, Yoshitaka , DAIMARU, Takuichiro , NAGAYASU, Hiromitsu
CPC分类号: B01D46/00 , B01D53/14 , B01D53/62 , B01D53/75 , B01D53/78 , B01D53/96 , C01B32/50 , F23J15/06
摘要: The objective of the present invention is to treat waste water appropriately. This CO2 recovery system comprises: a combustion facility; a dust collector into which exhaust gas containing CO2, discharged from the combustion facility, is introduced, and which removes solid components from the exhaust gas; an exhaust gas cooling device into which the exhaust gas is introduced, and which cools the exhaust gas by bringing the same into contact with cooling water; a CO2 absorption tower into which the exhaust gas cooled by the exhaust gas cooling device is introduced, and which removes the CO2 from the exhaust gas by bringing the exhaust gas into contact with a CO2 absorbent; and a cooling water introduction line which is connected to the exhaust gas cooling device and to a supply site, which is a site on an upstream side, in the flow of exhaust gas, of the dust collector, and which guides at least a portion of the cooling water inside the exhaust gas cooling device to the supply site.
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公开(公告)号:EP4208282B1
公开(公告)日:2024-06-26
申请号:EP21766167.7
申请日:2021-08-25
CPC分类号: B01D53/80 , B01D53/96 , B01D2251/30420130101 , B01D2251/60620130101 , B01D53/75 , B01D2258/02520130101 , Y02P10/20
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公开(公告)号:EP4378887A1
公开(公告)日:2024-06-05
申请号:EP22383163.7
申请日:2022-12-01
IPC分类号: C01B3/16 , B01D53/62 , B01D53/96 , B01J23/72 , B01J23/745 , C01B3/18 , C01F11/06 , C01F11/18 , C10K3/02 , B01J8/08 , B01J8/18 , B01J8/24 , B01J8/38
CPC分类号: C01B3/16 , C10K3/026 , C01F11/06 , C01F11/18 , C01B3/18 , B01D53/62 , B01D53/96 , B01J23/745 , B01J23/72 , B01J8/08 , B01J8/1827 , B01J8/1863 , B01J8/24 , B01J8/38 , B01D2257/50420130101 , B01D2251/40420130101 , B01D2251/60220130101 , B01D2251/20220130101 , B01D53/83
摘要: This invention discloses a hydrogenation method of CaCO3 with H2 to produce CaO and a syngas product gas containing H2, CO, CO2 and H2O, preferably with a H2/CO mol ratio close to 2. The method operates by arranging a solids containing CaCO3 and at least CaO (as reverse water gas shift catalyst) in a reactor, heating them to a temperature that depends on operating pressure and feeding H2 to react with them and cause a cooling of the solids while producing a syngas and a solids mixture containing an increased fracstion of CaO. The method operates continuously by cyclically recarbonating the CaO with the CO2 contained in a gas, or by feeding new CaCO3 to the bed of solids and extracting an equimolar quantity of CaO.
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公开(公告)号:EP3227246B1
公开(公告)日:2018-10-17
申请号:EP15804725.8
申请日:2015-11-30
申请人: L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude , Lafarge
发明人: PANIER, Faustine , PAUBEL, Xavier , RENNA, Carlo , GIMENEZ, Michel , PAXTON, Colin , WASSARD, Henrik , DRIVSHOLM, Morten , TSIAVA, Rémi
IPC分类号: C04B7/43
CPC分类号: C04B7/434 , B01D45/16 , B01D53/96 , C01B32/50 , C04B2/10 , F27B7/20 , F27B7/2033 , F27D17/004 , Y02P40/18
摘要: Method and installation for calcining cement raw meal in a calciner (10) whereby fuel and a calciner oxidant having an oxygen content of at least 30% vol are introduced into the calciner (10) so as to generate either an oxidant-lean zone or a fuel-lean zone in the calciner located between the lowermost fuel inlet level (L13) and the lowermost oxidant inlet level (L16) of the calciner (10), between 50% and 100% by weight of the raw meal (14, 15) being supplied to the calciner (10) upstream of and/or within the oxidant-lean, respectively the fuel-lean zone.
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公开(公告)号:EP2831033B1
公开(公告)日:2018-10-03
申请号:EP13768394.2
申请日:2013-03-28
申请人: HTC Purenergy Inc.
IPC分类号: C07C209/84 , B01D53/96 , B01D53/14 , B01D1/00
CPC分类号: C07C209/84 , B01D1/0064 , B01D1/0082 , B01D1/06 , B01D53/1425 , B01D53/1493 , B01D53/96 , B01D2252/204 , B01D2257/302 , B01D2257/304 , B01D2257/404 , B01D2257/504 , C07C213/10
摘要: A processes is for purifying an amine compound from a feed solvent which includes an amine salt of the amine compound. The process includes heating the feed solvent in a single stage evaporator of a reclaimer at a reduced operating pressure by feeding the evaporator with a constant amount of thermal energy; and evaporating the amine compound to purity the amine compound from the feed solvent.
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公开(公告)号:EP3362172A1
公开(公告)日:2018-08-22
申请号:EP15906359.3
申请日:2015-10-13
申请人: Tsapatsis, Michael , Balasubramanian, Veerappan Vaithilingam , Wahedi, Yasser Al , Hashimi, Al , Regents of the University of Minnesota , Regents of the University of Minnesota
IPC分类号: B01J20/06
CPC分类号: B01J20/08 , B01D53/52 , B01D53/82 , B01D53/96 , B01D2253/1124 , B01D2257/304 , B01J20/0281 , B01J20/0285 , B01J20/041 , B01J20/103 , B01J20/2803 , B01J20/3433 , B01J20/3458 , B01J2220/42
摘要: An example method of removing hydrogen sulfide from an input gas includes exposing an adsorbent material to an input gas to obtain an output gas. A concentration of hydrogen sulfide of the output gas is less than a concentration of hydrogen sulfide of the input gas. The adsorbent material includes copper oxide, magnesium oxide, and aluminum oxide. An atomic ratio of copper to magnesium to aluminum of the adsorbent material is X:Y:Z, where X is greater than or equal to 0.6 and less than or equal to 0.9, where Y is greater than or equal to 0 and less than or equal to 0.2, where Z is greater than or equal to 0 and less than or equal to 0.2, and where X+Y+Z is equal to 1.
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公开(公告)号:EP3272412A4
公开(公告)日:2018-07-18
申请号:EP16767678
申请日:2016-03-09
发明人: WEI XIONGHUI
CPC分类号: B01D53/1487 , B01D53/1462 , B01D53/56 , B01D53/565 , B01D53/78 , B01D53/96 , B01D2251/10 , B01D2251/102 , B01D2251/104 , B01D2251/106 , B01D2251/30 , B01D2251/40 , B01D2252/10 , B01D2252/2026 , B01D2252/204 , B01D2252/602 , B01D2255/2025 , B01D2257/404 , B01D2258/0283 , Y02A50/2345
摘要: A process and an apparatus for gas denitration, involving first the use of an oxidizing agent to oxidize NO in a gas to NO 2 , then using a denitration agent to absorb the NO 2 in the gas, thus achieving the purpose of denitration.
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9.
公开(公告)号:EP3341590A1
公开(公告)日:2018-07-04
申请号:EP16757529.9
申请日:2016-08-23
IPC分类号: F01K25/08
CPC分类号: F28D7/0083 , B01D3/007 , B01D3/32 , B01D51/10 , B01D53/047 , B01D53/1462 , B01D53/185 , B01D53/343 , B01D53/48 , B01D53/8603 , B01D53/96 , B01D2252/204 , C01B3/24 , C01B2203/0233 , C02F1/586 , C02F2101/10 , C02F2101/101 , C02F2101/16 , C02F2103/18 , C02F2103/36 , C07C7/08 , C10G33/06 , C10G35/04 , C10G45/00 , C10G45/02 , C10G45/44 , C10G47/00 , C10G65/00 , C10G65/12 , C10G69/00 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4056 , C10G2400/04 , C10G2400/30 , C10K3/04 , C10L3/101 , C10L3/103 , C10L3/104 , C10L2290/06 , C10L2290/541 , F01D17/145 , F01K3/185 , F01K13/00 , F01K13/02 , F01K23/06 , F01K23/064 , F01K25/06 , F01K25/08 , F01K27/00 , F01K27/02 , F28F9/26 , H02K7/1823 , Y02P20/129 , Y02P30/10
摘要: Configurations and related processing schemes of specific inter-plants and hybrid, intra- and inter-plants waste heat recovery schemes for thermal energy consumption reduction in integrated refining-petrochemical facilities synthesized for grassroots medium grade crude oil semi-conversion refineries to increase energy efficiency from specific portions of low grade waste heat sources are described. Configurations and related processing schemes of specific inter-plants and hybrid, intra- and inter-plants waste heat recovery schemes for thermal energy consumption reduction in integrated refining-petrochemical facilities synthesized for integrated medium grade crude oil semi-conversion refineries and aromatics complex for increasing energy efficiency from specific portions of low grade waste sources are also described.
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公开(公告)号:EP3341580A1
公开(公告)日:2018-07-04
申请号:EP16760275.4
申请日:2016-08-22
CPC分类号: F28D7/0083 , B01D3/007 , B01D3/32 , B01D51/10 , B01D53/047 , B01D53/1462 , B01D53/185 , B01D53/343 , B01D53/48 , B01D53/8603 , B01D53/96 , B01D2252/204 , C01B3/24 , C01B2203/0233 , C02F1/586 , C02F2101/10 , C02F2101/101 , C02F2101/16 , C02F2103/18 , C02F2103/36 , C07C7/08 , C10G33/06 , C10G35/04 , C10G45/00 , C10G45/02 , C10G45/44 , C10G47/00 , C10G65/00 , C10G65/12 , C10G69/00 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4056 , C10G2400/04 , C10G2400/30 , C10K3/04 , C10L3/101 , C10L3/103 , C10L3/104 , C10L2290/06 , C10L2290/541 , F01D17/145 , F01K3/185 , F01K13/00 , F01K13/02 , F01K23/06 , F01K23/064 , F01K25/06 , F01K25/08 , F01K27/00 , F01K27/02 , F28F9/26 , H02K7/1823 , Y02P20/129 , Y02P30/10
摘要: Configurations and related processing schemes of specific inter-plants and hybrid, intra- and inter-plants waste heat recovery schemes for thermal energy consumption reduction in integrated refining-petrochemical facilities synthesized for grassroots medium grade crude oil semi-conversion refineries to increase energy efficiency from specific portions of low grade waste heat sources are described. Configurations and related processing schemes of specific inter-plants and hybrid, intra- and inter-plants waste heat recovery schemes for thermal energy consumption reduction in integrated refining-petrochemical facilities synthesized for integrated medium grade crude oil semi-conversion refineries and aromatics complex for increasing energy efficiency from specific portions of low grade waste sources are also described.
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