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    PARTICLE SEPARATION DEVICE FOR CHEMICAL LOOPING COMBUSTION LOOP
    1.
    发明申请
    PARTICLE SEPARATION DEVICE FOR CHEMICAL LOOPING COMBUSTION LOOP 审中-公开
    用于化学循环燃烧循环的颗粒分离装置

    公开(公告)号：WO2011151537A3

    公开(公告)日：2012-01-26

    申请号：PCT/FR2011000317

    申请日：2011-05-27

    Applicant: IFP ENERGIES NOUVELLES ,  TOTAL SA ,  HOTEIT ALI ,  GUILLOU FLORENT ,  RIFFLART SEBASTIEN ,  GAUTHIER THIERRY

    Inventor： HOTEIT ALI ,  GUILLOU FLORENT ,  RIFFLART SEBASTIEN ,  GAUTHIER THIERRY

    IPC: F23C99/00 ,  B01D49/00 ,  B01J8/26 ,  F23C10/00 ,  F23C10/10

    CPC classification number: F23C10/10 ,  F23C10/005 ,  F23C99/00 ,  F23C2900/99008 ,  F23J2217/60 ,  Y02E20/346

    Abstract: The invention relates to a chemical looping combustion device which uses a solid fuel that generates particles of unburned residues and which employs oxygen-carrying particles, such as metal oxides. The device comprises at least one combustion zone and a separator for separating the particles contained in a gaseous mixture originating from the combustion zone. The separator comprises at least one enclosure (1) including an intake passage (4) for the mixture, a discharge passage (5) located in the lower part of the enclosure and an outlet passage (6) located in the upper part of the device, the intake and discharge/outlet parameters being selected in order to create a dense phase in the lower part of the enclosure and a diluted phase in the upper part thereof. The invention also relates to a combustion method using the device of the invention.

    Abstract translation: 本发明涉及一种化学循环燃烧装置，其使用产生未燃残余物颗粒的固体燃料，并且其使用诸如金属氧化物的载氧颗粒。 该装置包括至少一个燃烧区和分离器，用于分离源自燃烧区的气态混合物中所含的颗粒。 分离器包括至少一个包括用于混合物的进气通道（4）的外壳（1），位于外壳下部的排放通道（5）和位于设备的上部的出口通道（6） 为了在外壳的下部产生密相，并且在其上部具有稀相，选择进气和排出/出口参数。 本发明还涉及使用本发明的装置的燃烧方法。

    INTEGRATED OXIDATION, REDUCTION, AND GASIFICATION METHOD FOR PRODUCING A SYNTHETIC GAS AND ENERGY IN A CHEMICAL LOOP
    3.
    发明申请
    INTEGRATED OXIDATION, REDUCTION, AND GASIFICATION METHOD FOR PRODUCING A SYNTHETIC GAS AND ENERGY IN A CHEMICAL LOOP 审中-公开
    一体化氧化，还原和气化方法，用于生产合成气和化学循环中的能量

    公开(公告)号：WO2010086529A9

    公开(公告)日：2011-09-29

    申请号：PCT/FR2010000069

    申请日：2010-01-28

    Applicant: IFP ENERGIES NOUVELLES ,  TOTAL SA ,  HOTEIT ALI ,  GUILLOU FLORENT ,  FORRET ANN ,  GAUTHIER THIERRY

    Inventor： HOTEIT ALI ,  GUILLOU FLORENT ,  FORRET ANN ,  GAUTHIER THIERRY

    IPC: C10J3/00

    CPC classification number: C01B3/42 ,  C01B3/48 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/1041 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1247 ,  C01B2203/84 ,  C01B2203/86 ,  C10J3/725 ,  C10J2300/1659 ,  C10K3/04 ,  Y02P30/30

    Abstract: The invention relates to a method for producing synthetic gas in at least one chemical loop, which is self-sufficient in terms of energy. The chemical loop includes at least three separate reaction areas for oxidation, reduction, and gasification: 1. at least one oxidation reaction area R1 supplied with air, referred to as an air reactor, in which the oxidation reaction of metal oxides after reduction is carried out; 2. at least one reduction by combustion reaction area R2, referred to as a fuel oil reactor, in which the combustion reaction of the charges in the presence of the oxygen present in the metal oxides is carried out; 3. at least one gasification reaction area R3, referred to as a gasification reactor, for the solid and/or liquid feedstock for producing a synthesis gas, said gasification being catalysed by the at least partially reduced metal oxides from R2.

    Abstract translation: 本发明涉及一种在能量方面是自给自足的至少一种化学回路中生产合成气体的方法。 化学回路包括用于氧化，还原和气化的至少三个独立的反应区域：1.至少一个供给空气的氧化反应区域R1（称为空气反应器），其中负载还原后的金属氧化物的氧化反应 出; 燃烧反应区域R2称为燃料油反应器，在金属氧化物中存在的氧存在下电荷的燃烧反应进行至少一次还原; 3.用于固体和/或液体原料的至少一个称为气化反应器的气化反应区域R3，用于生产合成气，所述气化由R2中至少部分还原的金属氧化物催化。

    CHEMICAL LOOPING COMBUSTION METHOD WITH THE DILUTED-PHASE REMOVAL OF ASH AND FINES IN THE OXIDATION ZONE, AND FACILITY USING SUCH A METHOD
    5.
    发明申请
    CHEMICAL LOOPING COMBUSTION METHOD WITH THE DILUTED-PHASE REMOVAL OF ASH AND FINES IN THE OXIDATION ZONE, AND FACILITY USING SUCH A METHOD 审中-公开
    化学循环燃烧法，稀释相去除氧化区中的灰和粉末，以及使用这种方法的设备

    公开(公告)号：WO2013079817A3

    公开(公告)日：2013-07-25

    申请号：PCT/FR2012000432

    申请日：2012-10-25

    Applicant: IFP ENERGIES NOUVELLES

    Inventor： GUILLOU FLORENT ,  GAUTHIER THIERRY ,  HOTEIT ALI ,  RIFFLART SEBASTIEN

    IPC: F23C10/00 ,  F23C10/26

    CPC classification number: F23C10/01 ,  F23C10/005 ,  F23C10/08 ,  F23C10/24 ,  F23C10/26 ,  F23C2900/10003 ,  F23C2900/99008 ,  Y02E20/346

    Abstract: The invention relates to a method for the chemical looping combustion of a solid hydrocarbon feedstock, in which: particles of oxygen-carrying material originating from a reduction zone (RO) are brought into contact with a flow of oxidising gas in a reactive oxidation zone (R1); and the fly ash, the fines and the particles of oxygen carrying material in the mixture originating from zone R1 are separated in a diluted-phase separation zone (S2), the driving force required for diluted-phase elutriation in S2 being provided by the flow of oxidising gas from the reactive oxidation zone (R1). Optionally, enhanced separation is performed in a dust removal zone (S4) and, optionally, subsequently in a dense-phase elutriation separation zone (S5). The invention also relates to a chemical looping combustion facility that can be used to perform the aforementioned method.

    Abstract translation: 本发明涉及一种用于固体烃原料化学循环燃烧的方法，其中：使源自还原区（RO）的携氧材料颗粒与氧化气体流在反应性氧化区（ R1）; 并且来自区域R1的混合物中的飞灰，细粒和携氧物质颗粒在稀相分离区（S2）中分离，S2中由稀释相淘析所需的驱动力由流提供 来自反应氧化区（R1）的氧化气体。 任选地，在除尘区（S4）中并且任选地随后在密相淘选分离区（S5）中进行增强的分离。 本发明还涉及可用于执行上述方法的化学循环燃烧设施。

    OPTIMISED METHOD AND DEVICE FOR CHEMICAL LOOP COMBUSTION ON LIQUID HYDROCARBON FEEDSTOCK
    6.
    发明申请
    OPTIMISED METHOD AND DEVICE FOR CHEMICAL LOOP COMBUSTION ON LIQUID HYDROCARBON FEEDSTOCK 审中-公开
    液化石油气化学循环燃烧优化方法及装置

    公开(公告)号：WO2010034900A3

    公开(公告)日：2011-03-03

    申请号：PCT/FR2009001113

    申请日：2009-09-21

    Applicant: IFP ENERGIES NOUVELLES ,  GAUTHIER THIERRY ,  HOTEIT ALI ,  FORRET ANN ,  TOTAL SA

    Inventor： GAUTHIER THIERRY ,  HOTEIT ALI ,  FORRET ANN

    IPC: F23C99/00 ,  F24V30/00 ,  C10G11/18 ,  F23C10/00 ,  F23C10/01

    CPC classification number: F23C99/00 ,  B01J8/26 ,  B01J8/388 ,  B01J2208/00902 ,  F23C10/005 ,  F23C10/01 ,  F23C2900/99008 ,  Y02E20/346

    Abstract: The invention relates to a device and an improved method for the chemical loop combustion of at least one liquid hydrocarbon feedstock, said method comprising: mixing the liquid feedstock with an atomisation gas for feeding the same into a metal oxide transport area (2) upstream from the combustion area (3) and through an atomisation means (6) so as to form finely dispersed liquid droplets in the atomisation gas; spraying the liquid feedstock in the form of droplets into contact with at least one portion of the metal oxides in the transport area (2), the operational conditions in the transport area (2) being selected so that the superficial speed of the gas after spraying the liquid feedstock is higher than the transport speed of the metal oxide particles; and feeding the entirety of the effluents from the transport area (2) towards a combustion area (3) for reducing the metal oxides, said combustion area (3) including at least one dense-phase fluidised bed. The invention can advantageously be used for capturing CO2 and for generating power.

    Abstract translation: 本发明涉及一种用于至少一种液态烃原料的化学回路燃烧的装置和改进的方法，所述方法包括：将液体原料与雾化气体混合，以将其送入金属氧化物输送区域（2）的上游 燃烧区域（3）并通过雾化装置（6），以在雾化气体中形成精细分散的液滴; 以液滴的形式喷射液体原料与输送区域（2）中的金属氧化物的至少一部分接触，选择输送区域（2）中的操作条件使得喷涂后气体的表观速度 液体原料高于金属氧化物颗粒的输送速度; 以及从所述输送区域（2）向所述燃烧区域（3）供给整个所述废气以还原所述金属氧化物，所述燃烧区域（3）包括至少一个密相流化床。 本发明可有利地用于捕获CO 2和用于发电。

    METHOD FOR SORTING SPENT CATALYST DEPENDING ON THE METALS OF THE CATALYST
    7.
    发明专利
    METHOD FOR SORTING SPENT CATALYST DEPENDING ON THE METALS OF THE CATALYST 未知

    公开(公告)号：SG11201604122QA

    公开(公告)日：2016-07-28

    申请号：SG11201604122Q

    申请日：2014-12-01

    Applicant: IFP ENERGIES NOUVELLES

    Inventor： GAUTHIER THIERRY ,  LIENEMANN CHARLES-PHILIPPE

    IPC: B01J38/72 ,  B01J23/75 ,  B01J23/755 ,  B01J23/88 ,  B01J23/888 ,  B07C5/342 ,  G01N21/71

    Abstract: The invention concerns a method for separating at least one catalyst from a mixture of catalysts homogeneous in shape, the catalysts comprising at least one metal chosen from the group formed by Ni, Co, Mo, W, the catalyst to be separated comprising a characteristic metal chosen from the group formed by Ni, Co, Mo, W and the other catalysts of the mixture not containing said characteristic metal, method in which - the catalyst grains of said mixture move past the LIBS (Laser Induced Breakdown Spectrometry) detection system • - the presence of said characteristic metal in the catalysts is detected by the LIBS technique, the wavelength being chosen to detect said characteristic metal • - the LIBS detection system sends a signal to a means for discharging the grains of the catalyst to be separated so as to separate said grains from the other catalysts of said mixture. The invention also concerns the associated device.

    PROCEDE DE TRI DE CATALYSEUR USE EN FONCTION DES METAUX DU CATALYSEUR
    10.
    发明专利
    PROCEDE DE TRI DE CATALYSEUR USE EN FONCTION DES METAUX DU CATALYSEUR 未知

    公开(公告)号：FR3014333A1

    公开(公告)日：2015-06-12

    申请号：FR1362225

    申请日：2013-12-06

    Applicant: IFP ENERGIES NOUVELLES

    Inventor： GAUTHIER THIERRY ,  LIENEMANN CHARLES-PHILIPPE

    IPC: B01J38/72 ,  B01J23/75 ,  B01J23/755 ,  B01J23/88 ,  B01J23/888 ,  B07C5/342

    Abstract: L'invention concerne un procédé de séparation d'au moins un catalyseur d'un mélange de catalyseurs de forme homogène, les catalyseurs comprenant au moins un métal choisi dans le groupe formé par Ni, Co, Mo, W, le catalyseur à séparer comprenant un métal caractéristique choisi dans le groupe formé par Ni, Co, Mo, W et les autres catalyseurs du mélange ne contenant pas ledit métal caractéristique, procédé dans lequel -les grains de catalyseurs dudit mélange passent devant le système de détection LIBS -la présence dudit métal caractéristique dans les catalyseurs est détectée par la technique LIBS, la longueur d'onde étant choisie pour détecter ledit métal caractéristique -le système de détection LIBS envoie un signal vers un moyen d'évacuation des grains du catalyseur à séparer de façon à séparer lesdits grains des autres catalyseurs dudit mélange.

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