专利检索 ap:("IFP Énergies nouvelles" OR "Total Raffinage Chimie") AND inv:"SOZINHO, Tiago" 第 1 页

1.

发明公开
PROCÉDÉ ET INSTALLATION DE COMBUSTION PAR OXYDO-RÉDUCTION EN BOUCLE CHIMIQUE D'UNE CHARGE HYDROCARBONÉE SOLIDE 有权
标题翻译：方法和系统刻录带有氧化还原对固体碳氢化合物FEED通过化学LOOP

公开(公告)号：EP3008384A1

公开(公告)日：2016-04-20

申请号：EP14734891.6

申请日：2014-06-12

申请人： IFP Énergies nouvelles , TOTAL RAFFINAGE CHIMIE

发明人： GUILLOU, Florent , SOZINHO, Tiago , DREUX, Heloise , STAINTON, Hélène

IPC分类号： F23C10/00 , F23C10/22 , F23C10/26

CPC分类号： F23C10/01 , F23C10/002 , F23C10/005 , F23C10/04 , F23C10/20 , F23C10/22 , F23C10/26 , F23C10/28 , F23C2900/99008 , F23D1/00 , Y02E20/346

摘要： The invention concerns a method and facility for CLC of a solid hydrocarbon feedstock which involves injecting the solid hydrocarbon feedstock in such a way as to limit any occurrence of the feedstock sticking to the walls of the injection device. The solid feedstock is introduced into a conveying area operating in a fluidised bed opening into a combustion reactor. A fluidising gas is injected into this conveying area, while controlling the flow of the gas such that the superficial gas velocity in the conveying area is greater than the terminal falling velocity of the particles of the solid hydrocarbon feedstock and the terminal falling velocity of solid particles located in the combustion reactor, and while controlling the temperature of the fluidising gas such that the temperature of the conveying area is less than or equal to 500
0 C.

摘要翻译： 本发明涉及一种方法和一种用于化学循环固体烃进料的燃烧CLC worin提议注入固体烃进料，以便限制供给到注射装置的壁的粘着的任何发生的装置。固体进料被送入流化床条件和开口到燃烧反应器下运行的输送区。流化气体被注入该传送区，同时控制在寻求一种方式气体的流动那样的气体在输送区中的表观速度是比固体烃进料粒子的终端速度和固体粒子的本终端速度更高在燃烧反应器中，而在寻求一种方式控制所述流化气体温度没有在传送区中的温度是小于或等于500℃。

2.

发明公开
PROCEDE ET INSTALLATION DE COMBUSTION PAR OXYDO-RÉDUCTION EN BOUCLE CHIMIQUE D'UNE CHARGE HYDROCARBONEE GAZEUSE AVEC VAPORÉFORMAGE CATALYTIQUE INTERMEDIAIRE DE LA CHARGE 有权
标题翻译：程序ET安装DE燃烧PAR氧化 - 反应锅炉CHIMIQUE D'UNE CHARGE HYDROCARBONEE GAZEUSE AVECVAPORÉFORMAGECATALYTIQUE INTERMEDIAIRE DE LA CHARGE

公开(公告)号：EP3230414A1

公开(公告)日：2017-10-18

申请号：EP15802138.6

申请日：2015-12-01

申请人： IFP Énergies nouvelles , Total Raffinage Chimie

发明人： SOZINHO, Tiago , YAZDANPANAH, Mahdi , GUILLOU, Florent , FORRET, Ann , BERTHOLIN, Stephane , STAINTON, Hélène

IPC分类号： C10J3/72 , B01J8/26 , C01B3/34

CPC分类号： C01B3/44 , B01J8/0055 , B01J8/1827 , B01J8/26 , B01J2208/00752 , B01J2208/00893 , C01B3/382 , C01B2203/0233 , C01B2203/0238 , C01B2203/025 , C01B2203/0255 , C01B2203/06 , C01B2203/1058 , C01B2203/1082 , C01B2203/1094 , C01B2203/1241 , F23C10/01 , F23C10/22 , F23C2900/99008 , Y02E20/346

摘要： The invention relates to a method and an apparatus for combustion by chemical-loop oxidation reduction (CLC) of a gaseous hydrocarbon feedstock, for example natural gas consisting essentially of methane. According to the invention, catalytic steam reforming of the feedstock is carried out between two consecutive steps of combustion of the feedstock in contact with an oxidation-reduction active mass in particle form. The reforming catalyst is placed in a fixed bed in a reforming zone (130) between the two reduction zones (120, 140) in which the two combustion steps are performed.

摘要翻译： 本发明涉及用于通过气态烃原料（例如主要由甲烷组成的天然气）的化学回路氧化还原（CLC）来燃烧的方法和设备。根据本发明，原料的催化蒸汽重整在与颗粒形式的氧化还原活性物质接触的原料的两个连续步骤之间进行。将重整催化剂置于其中进行两个燃烧步骤的两个还原区（120,140）之间的重整区（130）中的固定床中。

3.

发明公开
INSTALLATION ET PROCEDE DE COMBUSTION PAR OXYDO-RÉDUCTION EN BOUCLE CHIMIQUE D'UNE CHARGE HYDROCARBONEE GAZEUSE AVEC PRE- REFORMAGE CATALYTIQUE DE LA CHARGE 审中-公开
标题翻译：安装ET程序DE燃烧PAR氧化还原反应EN BOUCLE CHIMIQUE D'UNE CHARGE HYDROCARBONEE GAZEUSE AVEC PRE-重整催化剂DE LA CHARGE

公开(公告)号：EP3230416A1

公开(公告)日：2017-10-18

申请号：EP15805426.2

申请日：2015-12-01

申请人： IFP Énergies nouvelles , Total Raffinage Chimie

发明人： GUILLOU, Florent , FISCHER, Beatrice , SOZINHO, Tiago , CLOUPET, Ann , BERTHOLIN, Stephane , YAZDANPANAH, Mahdi , STAINTON, Hélène

IPC分类号： C10J3/72

CPC分类号： F23C10/01 , B01J8/065 , B01J8/067 , B01J8/24 , B01J2208/00495 , B01J2208/00504 , B01J2208/00911 , B01J2208/065 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/0822 , C01B2203/1058 , C01B2203/1241 , F23C10/005 , F23C10/04 , F23C10/20 , F23C10/22 , F23C2900/99008 , Y02E20/346

摘要： The invention relates to a plant and a process for chemical looping oxidation-reduction combustion of a gaseous hydrocarbon feedstock, for example natural gas essentially comprising methane. According to the invention, a catalytic pre-reforming of the feedstock is carried out in a prereforming zone comprising a fixed reforming catalyst, while benefiting from a heat transfer between the reduction or oxidation zone of the chemical loop and the prereforming zone adjacent to the reduction or oxidation zone. The prereforming zone (130) and the oxidation zone (110) or the prereforming zone (130) and the reduction zone (120) are thus thermally integrated within the same reactor (100) while being separated by at least one thermally conductive dividing wall (140).

摘要翻译： 本发明涉及用于气态烃原料（例如主要包含甲烷的天然气）的化学循环氧化还原燃烧的设备和方法。根据本发明，原料的催化预重整在包含固定重整催化剂的预重整区中进行，同时受益于化学回路的还原或氧化区与邻近还原的预重整区之间的热传递或氧化区。因此，预重整区（130）和氧化区（110）或预重整区（130）和还原区（120）被热结合在同一反应器（100）内，同时被至少一个导热分隔壁 140）。

4.

发明公开
PROCEDE ET INSTALLATION DE COMBUSTION PAR OXYDO-RÉDUCTION EN BOUCLE CHIMIQUE D'UNE CHARGE HYDROCARBONEE GAZEUSE AVEC REFORMAGE CATALYTIQUE IN SITU DE LA CHARGE 审中-公开
标题翻译：程序安装DE燃烧PAR氧化 - 反应EN BOUCLE CHIMIQUE D'UNE CHARGE HYDROCARBONEE GAZEUSE AVEC REFORMAGE CATALYTIQUE IN SITU DE LA CHARGE

公开(公告)号：EP3230415A1

公开(公告)日：2017-10-18

申请号：EP15802139.4

申请日：2015-12-01

申请人： IFP Énergies nouvelles , TOTAL RAFFINAGE CHIMIE

发明人： YAZDANPANAH, Mahdi , PELLETANT, William , SOZINHO, Tiago , BERTHOLIN, Stephane , STAINTON, Hélène , CLOUPET, Ann , GUILLOU, Florent

IPC分类号： C10J3/72 , B01J8/26 , C01B3/34

CPC分类号： F23C10/01 , B01J8/1827 , B01J8/26 , C01B3/44 , C01B2203/0227 , C01B2203/0233 , C01B2203/06 , C01B2203/1058 , C01B2203/1082 , C01B2203/1094 , C01B2203/1241 , F23C10/02 , F23C10/20 , F23C10/22 , F23C99/00 , F23C2900/99008 , Y02E20/346

摘要： The invention relates to a method and an apparatus for combustion by chemical-loop oxidation reduction (CLC) of a gaseous hydrocarbon feedstock, for example natural gas consisting essentially of methane. According to the invention, catalytic reforming of the feedstock is carried out within the reduction zone in which the combustion of the feedstock takes place, in contact with an oxidation-reduction active mass in particle form. The reforming catalyst is in the form of fluidised particles which are not transported within the reduction zone. The catalyst thus confined to the reduction zone does not circulate in the CLC loop.

摘要翻译： 本发明涉及用于通过气态烃原料（例如主要由甲烷组成的天然气）的化学回路氧化还原（CLC）来燃烧的方法和设备。根据本发明，原料的催化重整在其中进行原料燃烧的还原区内与颗粒形式的氧化还原活性物质接触。重整催化剂是不在还原区内输送的流化颗粒的形式。因此限制在还原区的催化剂不在CLC环路中循环。

5.

发明公开
PROCEDE ET DISPOSITIF DE COMBUSTION PAR BOUCLE CHIMIQUE DE CHARGES HYDROCARBONEES LIQUIDES 审中-公开
标题翻译：的方法和设备用于液体烃原料在化学CIRCUIT燃

公开(公告)号：EP2981350A1

公开(公告)日：2016-02-10

申请号：EP14715357.1

申请日：2014-03-11

申请人： IFP Énergies nouvelles , TOTAL RAFFINAGE CHIMIE

发明人： YAZDANPANAH, Mahdi , SOZINHO, Tiago , GAUTHIER, Thierry , GUILLOU, Florent

IPC分类号： B01J8/28 , B01J8/32 , B01J8/38 , B01J8/00 , F23C1/02 , F23C10/00

CPC分类号： F23C10/01 , B01J8/0055 , B01J8/007 , B01J8/28 , B01J8/32 , B01J8/388 , B01J2208/00513 , B01J2208/00902 , F23C6/04 , F23C10/005 , F23C10/10 , F23C10/22 , F23C2206/101 , F23C2900/10003 , F23C2900/99008 , Y02E20/346

摘要： The invention concerns a method of chemical-loop oxidation-reduction combustion (CLC) of liquid hydrocarbon feedstocks carried out in a fluidised bed, in which the liquid hydrocarbon feedstock (2) is partially vaporised in contact with a hot solid (1) in the form of particles to form a partially vaporised liquid feedstock and to form coke on said solid (1), before bringing the partially vaporised liquid feedstock (19) into contact with an oxidation-reduction active mass in the form of particles (12) to carry out the combustion of the partially vaporised liquid feedstock (19). The hot solid particles (1) used to carry the coke can, in particular, form a second particle circulation loop in the fluidised bed, the first being that of the particles of the oxygen-transporting oxidation-reduction active mass (12) flowing between the oxidation and combustion reactors, thus allowing the coke-carrying particles (1) to be recycled in the method.