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公开(公告)号:US20230183084A1
公开(公告)日:2023-06-15
申请号:US17921288
申请日:2021-04-07
申请人: CASALE SA
发明人: Iacopo CEREA , Ermanno FILIPPI , Flavio PEDON , Pasquale TALARICO
CPC分类号: C01C1/185 , B01J19/2415 , B01J19/02 , B01J2219/0218
摘要: A process of making ammonium nitrate from nitric acid and ammonia in a tubular reactor internally coated with a ceramic coating.
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公开(公告)号:US20160311680A1
公开(公告)日:2016-10-27
申请号:US15104448
申请日:2014-12-16
申请人: CASALE SA
发明人: Ermanno FILIPPI , Raffaele OSTUNI
CPC分类号: C01B3/025 , B01J7/02 , B01J19/0046 , B01J2219/0059 , B01J2219/00756 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/043 , C01B2203/046 , C01B2203/048 , C01B2203/143
摘要: A process and a related equipment for producing ammonia synthesis gas from a hydrocarbon-containing feedstock (20), the process comprising the steps of: primary reforming with steam (21), secondary reforming with an oxidant stream (23), and purification of the effluent of said secondary reforming, said purification comprising a step of shift conversion (13) of carbon monoxide, wherein the synthesis gas (25) produced by said secondary reforming is subject to a medium-temperature shift over a copper-based catalyst, and the global steam to carbon ratio of the process is not greater than 2.
摘要翻译: 一种用于从含烃原料(20)生产氨合成气的方法和相关设备,该方法包括以下步骤:用蒸汽(21)进行一次重整,用氧化剂流(23)进行二次重整,并纯化 所述二次重整的流出物,所述纯化包括一氧化碳的转移转化(13)的步骤,其中由所述二次转化产生的合成气(25)经受铜基催化剂的中温转变,并且 全球蒸汽碳比过程不大于2。
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公开(公告)号:US20200290869A1
公开(公告)日:2020-09-17
申请号:US16887191
申请日:2020-05-29
申请人: Casale SA
IPC分类号: C01B3/38 , C01B3/02 , C10K1/00 , C10J3/00 , C10J3/46 , B01D53/22 , B01J8/06 , C10J3/82 , F25J3/02
摘要: Process for manufacturing a hydrogen-containing synthesis gas from a natural gas feedstock, comprising the conversion of said natural gas into a raw product gas and purification of said product gas, the process having a heat input provided by combustion of a fuel; said process comprises a step of conversion of a carbonaceous feedstock, and at least a portion of said fuel is a gaseous fuel obtained by said step of conversion of said carbonaceous feedstock.
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公开(公告)号:US20190076805A1
公开(公告)日:2019-03-14
申请号:US16085116
申请日:2017-03-07
申请人: CASALE SA
发明人: Ermanno FILIPPI , Enrico RIZZI , Mirco TAROZZO
IPC分类号: B01J8/02
摘要: Radial or axial-radial flow catalytic chemical reactor comprising a cylindrical shell and at least one catalytic bed and comprising a plurality of perforated tubes, said tubes having an open end communicating with an inlet of a gaseous flow of reagents in the reactor, said tubes being provided with a plurality of holes on their side surface, said tubes being arranged around the catalytic bed so as to form an outer wall which bounds the catalytic bed and which distributes the reagents inside said bed; each of said tubes being formed by means of longitudinal or helical butt welding of a perforated strip.
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公开(公告)号:US20150307797A1
公开(公告)日:2015-10-29
申请号:US14790973
申请日:2015-07-02
申请人: Casale SA
发明人: Ermanno FILIPPI , Francesco BARATTO
CPC分类号: C10L3/08 , C01B3/586 , C01B2203/0445 , C01B2203/047 , C07C1/041 , C07C1/12 , C10G2/34 , C10G2300/1022 , C10G2300/4081 , C10G2300/807 , C10L2290/42 , Y02P20/582
摘要: A methanation section for producing substitute natural gas (SNG) by reacting a fresh syngas, the methanation section comprising adiabatic reactors connected in series, with heat removal and reacted gas-recirculation, wherein the fresh syngas is fed in parallel to said adiabatic reactors. In a preferred embodiment the reacted gas is recirculated to the first reactor and further dilution of the fresh gas at the inlet of the first and second reactor is achieved by steam addition.
摘要翻译: 用于通过使新鲜合成气(包括串联连接的绝热反应器的甲烷化部分)与除热和反应的气体再循环反应来生产替代天然气(SNG)的甲烷化部分,其中新鲜合成气平行于所述绝热反应器进料。 在优选的实施方案中,将反应的气体再循环到第一反应器中,并且通过蒸汽添加实现在第一和第二反应器的入口处的新鲜气体的进一步稀释。
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公开(公告)号:US20240101417A1
公开(公告)日:2024-03-28
申请号:US18271394
申请日:2022-01-20
申请人: Casale SA
发明人: Ermanno FILIPPI , Raffaele OSTUNI , Sergio PANZA
IPC分类号: C01B3/38 , B01D53/047 , C01B3/48 , C01B3/56 , C01C1/04 , C07C29/151
CPC分类号: C01B3/382 , B01D53/047 , C01B3/48 , C01B3/56 , C01C1/0405 , C07C29/1518 , B01D2256/16 , B01D2257/504 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/042 , C01B2203/0475 , C01B2203/061 , C01B2203/068 , C01B2203/0816 , C01B2203/1235 , C01B2203/142
摘要: Method for preparing a synthesis gas suitable for the synthesis of ammonia or methanol, the method comprises the step of feeding to the radiant portion of a primary reformer an oxygen-enriched air obtained by mixing air with an oxygen stream generated by water electrolysis.
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公开(公告)号:US20180072580A1
公开(公告)日:2018-03-15
申请号:US15637547
申请日:2017-06-29
申请人: Casale SA
CPC分类号: C01C1/0441 , C01B3/025 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/506 , C01B3/52 , C01B3/56 , C01B3/586 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0445 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/068 , C01B2203/1241 , C01B2203/142 , C01B2203/143 , C01B2203/147
摘要: A process for producing ammonia synthesis gas from the reforming of hydrocarbons with steam in a primary reformer (1) equipped with a plurality of externally heated catalytic tubes and then together with air in a secondary reformer (2) is characterized in that the reaction of said hydrocarbons with said steam in said primary reformer (1) is performed at an operating pressure of more than 35 bar in the catalytic tubes, in that air is added to said secondary reformer in excess over the nitrogen amount required for ammonia synthesis and in that the excess of nitrogen is removed downstream the secondary reformer preferably by cryogenic separation or by molecular sieves of the TAS or PSA type. This process allows to obtain high synthesis gas production capacities and lower investment and energy costs.
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公开(公告)号:US20180044192A1
公开(公告)日:2018-02-15
申请号:US15552054
申请日:2016-01-27
申请人: Casale SA
发明人: Ermanno FILIPPI , Raffaele OSTUNI
CPC分类号: C01C1/0441 , B01J8/06 , B01J2208/02 , B01J2208/06 , C01B3/025 , C01B2203/0233 , C01B2203/0244 , C01B2203/0405 , C01B2203/0415 , C01B2203/0495 , C01B2203/068 , C01B2203/142 , C01B2203/84 , C01C1/0405 , C01C1/0476 , C22C38/00 , C22C38/40 , Y02P20/52
摘要: Process and plant for the synthesis of ammonia from a hydrocarbon feedstock, comprising: primary reforming with steam and air-fired secondary reforming wherein primary reforming is performed at a temperature and pressure of at least 790° C. and 50 bar, and secondary reforming is carried out substantially in absence of excess air, the so obtained make-up synthesis gas having a H2 to N2 molar ratio in the range 2.5 to 3.
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公开(公告)号:US20170349435A1
公开(公告)日:2017-12-07
申请号:US15524845
申请日:2015-10-06
申请人: Casale SA
摘要: Process for manufacturing a hydrogen-containing synthesis gas from a natural gas feedstock, comprising the conversion of said natural gas into a raw product gas and purification of said product gas, the process having a heat input provided by combustion of a fuel; said process comprises a step of conversion of a carbonaceous feedstock, and at least a portion of said fuel is a gaseous fuel obtained by said step of conversion of said carbonaceous feedstock.
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公开(公告)号:US20170189874A1
公开(公告)日:2017-07-06
申请号:US15324982
申请日:2015-06-19
申请人: CASALE SA
发明人: Ermanno FILIPPI , Enrico RIZZI
IPC分类号: B01J8/02
CPC分类号: B01J8/0285 , B01J8/0035 , B01J8/0214 , B01J8/025 , B01J2208/0015 , B01J2208/00814 , B01J2208/022 , B01J2219/182 , B01J2219/1943 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2481
摘要: Horizontal reactor (1) for catalytic reactions, comprising an outer cylindrical shell (2), a catalytic bed (5) and heat exchange plates (6) immersed in said catalytic bed, parallel to each other and supplied with a heat exchange fluid; said reactor comprises a container (7) for said catalytic bed (5) and said plates (6), said container is extractable slidably from said shell, by means of at least one linear guide (31, 32, 45) extended longitudinally with respect to said shell (2).
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