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    • 12. 发明申请
    • METHOD OF HYDROTREATING FEEDS FROM RENEWABLE SOURCES WITH INDIRECT HEATING USING A CATALYST BASED ON MOLYBDENUM
    • 使用基于钼的催化剂对具有间接加热的可再生来源的进料进行加氢的方法
    • US20110094149A1
    • 2011-04-28
    • US12912025
    • 2010-10-26
    • Wilfried WeissLaurent BournayThierry ChapusAntoine Daudin
    • Wilfried WeissLaurent BournayThierry ChapusAntoine Daudin
    • C10L1/188
    • C10G65/04C10G3/46C10G3/48C10G3/50C10G2300/1014C10G2300/1018C10G2300/4006C10G2300/4081Y02P30/20
    • The invention describes a method of treating feeds from renewable sources comprising a hydrotreatment stage comprising at least two catalytic zones in which the entry stream comprising said feed mixed with at least a part of a hydrotreated liquid effluent from stage b) is introduced into the first catalytic zone at a temperature comprised between 150 and 260° C., and the effluent from the first catalytic zone is then introduced, mixed with at least a part of a hydrotreated liquid effluent from stage b) and preheated, into the following catalytic zone or zones at a temperature comprised between 260 and 320° C., and a stage of separation of the effluent from the hydrotreatment stage permitting the separation of a gaseous effluent and a hydrotreated liquid effluent of which at least a part is recycled at the top of each catalytic zone, said method using, in at least the catalytic zone or zones following the first, a bulk or supported catalyst comprising an active phase constituted by a sulphidized group VIB element, the group VIB element being molybdenum.
    • 本发明描述了一种处理来自可再生来源的饲料的方法,该方法包括加氢处理阶段,该加氢处理阶段包括至少两个催化区,其中将包含所述进料的进料与至少一部分来自步骤b)的加氢处理液体流出物混合进入第一催化剂 区域,然后引入来自第一催化区域的流出物,与来自阶段b)的加氢处理的液体流出物的至少一部分混合并预热到以下催化区或区域 在260至320℃之间的温度下,流出物与加氢处理阶段的分离阶段允许分离气态流出物和加氢处理的液体流出物,其中至少一部分在每个催化剂的顶部被再循环 所述方法在至少在第一个催化区域之后使用主体或负载的催化剂,其包含由 硫化VIB族元素,VIB族元素为钼。
    • 13. 发明授权
    • Flexible process for transformation of ethanol into middle distillates
    • 将乙醇转化为中间馏分的灵活过程
    • US09475999B2
    • 2016-10-25
    • US13102283
    • 2011-05-06
    • Emmanuelle GuillonNicolas CadranNatacha TouchaisLaurent Bournay
    • Emmanuelle GuillonNicolas CadranNatacha TouchaisLaurent Bournay
    • C07C1/24C10G3/00C10G50/00
    • C10G50/00C10G3/49C10G3/62C10G2300/1014C10G2300/301C10G2300/4018C10G2300/4081C10G2400/04C10G2400/08C10G2400/20C10G2400/22C10G2400/28Y02E50/13Y02P30/20
    • The invention describes a process for the production of middle distillate hydrocarbon bases from an ethanol feedstock that is produced from a renewable source that is obtained from biomass, whereby said process comprises a stage for purification of said feedstock, a stage for transformation of said purified feedstock into a light olefinic effluent that comprises at least 30% by weight of olefins that have between four to six carbon atoms relative to the total mass of the formed hydrocarbon compounds, whereby said stage works in the presence of a catalyst that comprises at least one zeolite that is selected from among the zeolites that have a structural type that appears in the following list: CHA, ERI, MTF, AEI, AEL, FER, EUO, MEL, MFS, TON, MTT and the zeolites ZBM-30, ZSM-48, IM-5 and IZM-2, taken by themselves or in a mixture, a stage for separation of the olefinic effluent that is obtained from stage b) in such a way as to eliminate at least a portion of the water that is formed during stage b) to produce at least one hydrocarbon gaseous effluent that for the most part has three or fewer carbon atoms and at least one olefinic hydrocarbon liquid effluent that for the most part has more than four carbon atoms, and a stage for oligomerization of at least a portion of the hydrocarbon effluents that are obtained from stage c) in the presence of an amorphous or zeolitic catalyst that has at least pore openings that contain 10 or 12 oxygen atoms, producing middle distillate hydrocarbon bases.
    • 本发明描述了从由生物质获得的可再生来源生产的乙醇原料生产中间馏分烃碱的方法,其中所述方法包括纯化所述原料的阶段,用于转化所述纯化原料的阶段 包含至少30重量%的具有4-6个碳原子的烯烃相对于形成的烃化合物的总质量的轻质烯烃流出物,其中所述阶段在包含至少一种沸石 选自具有下列结构类型的沸石:CHA,ERI,MTF,AEI,AEL,FER,EUO,MEL,MFS,TON,MTT和沸石ZBM-30,ZSM-48 ,IM-5和IZM-2,它们本身或在混合物中,分离从阶段b)获得的烯烃流出物的阶段,以消除形成的至少一部分水 环状阶段b)以产生至少一种大多数具有三个或更少碳原子的烃气态流出物和至少一种大多数具有四个以上碳原子的烯烃液体流出物, 至少一部分烃阶段c)在无定形或沸石催化剂存在下得到的烃流出物至少具有含有10或12个氧原子的孔隙,产生中间馏分烃基。
    • 17. 发明申请
    • METHOD OF HYDROTREATING FEEDS FROM RENEWABLE SOURCES WITH INDIRECT HEATING USING A CATALYST BASED ON NICKEL AND MOLYBDENUM HAVING A PARTICULAR ATOMIC RATIO
    • 使用基于镍的催化剂和具有特定原子比的钼的间接加热从可再生来源进料的方法
    • US20110098494A1
    • 2011-04-28
    • US12911983
    • 2010-10-26
    • Wilfried WEISSLaurent BournayThierry ChapusAntoine Daudin
    • Wilfried WEISSLaurent BournayThierry ChapusAntoine Daudin
    • C11B3/02
    • C10G3/46C10G3/48C10G3/50C10G65/04C10G2300/1014C10G2300/1018C10G2300/4006C10G2300/4081Y02P30/20
    • The invention describes a method of treating feeds from renewable sources comprising a hydrotreatment stage comprising at least two catalytic zones in which the entry stream comprising said feed mixed with at least a part of a hydrotreated liquid effluent from stage b) is introduced into the first catalytic zone at a temperature comprised between 150 and 260° C., and the effluent from the first catalytic zone is then introduced, mixed with at least a part of a hydrotreated liquid effluent from stage b) and preheated, into the following catalytic zone or zones at a temperature comprised between 260 and 320° C., and a stage of separation of the effluent from the hydrotreatment stage permitting the separation of a gaseous effluent and a hydrotreated liquid effluent of which at least a part is recycled at the top of each catalytic zone, said method using, in at least the catalytic zone or zones following the first, a bulk or supported catalyst comprising an active phase constituted by at least one group VIB element and at least one group VIII element, said elements being in sulphide form and the atomic ratio of the group VIII metal to the group VIB metal being strictly greater than 0 and less than 0.095.
    • 本发明描述了一种处理来自可再生来源的饲料的方法,该方法包括加氢处理阶段,该加氢处理阶段包括至少两个催化区,其中将包含所述进料的进料与至少一部分来自步骤b)的加氢处理液体流出物混合进入第一催化剂 区域,然后引入来自第一催化区域的流出物,与来自阶段b)的加氢处理的液体流出物的至少一部分混合并预热到以下催化区或区域 在260至320℃之间的温度下,流出物与加氢处理阶段的分离阶段允许分离气态流出物和加氢处理的液体流出物,其中至少一部分在每个催化剂的顶部被再循环 所述方法在至少在第一个催化区域之后使用本体或负载型催化剂,其包含由下式构成的活性相: 至少一种VIB族元素和至少一种VIII族元素,所述元素为硫化物形式,并且VIII族金属与VIB族金属的原子比严格大于0且小于0.095。