Method for reactivating catalysts used in catalytic vapor phase process
for producing dihydrocarbyl carbonates
    91.
    发明授权
    Method for reactivating catalysts used in catalytic vapor phase process for producing dihydrocarbyl carbonates 失效
    用于催化气相法生产二烃基碳酸酯的催化剂再活化方法

    公开(公告)号:US5132259A

    公开(公告)日:1992-07-21

    申请号:US688464

    申请日:1991-03-01

    申请人: Gerald L. Curnutt

    发明人: Gerald L. Curnutt

    CPC分类号: C07C68/005 Y02P20/584

    摘要: A process for the preparation of dihydrocarbyl carbonates comprising contacting an alkanol such as methanol, carbon monoxide and oxygen with a heterogeneous catalyst which comprises a metal halide such as cupric chloride or a mixed metal halide such as cupric chloride/potassium chloride impregnated on an appropriate support such as activated carbon; and a process for reactivating metal halide catalysts supported on porous carrier materials comprising drying and then contacting the supported catalysts with a gaseous stream of hydrogen halide for a period of time which is sufficient to convert all of the metal present in whatever form to the corresponding metal halide.

    摘要翻译: 一种制备二烃基碳酸酯的方法,包括使烷醇如甲醇,一氧化碳和氧气与非均相催化剂接触,所述非均相催化剂包括金属卤化物如氯化铜或混合金属卤化物如氯化铜/氯化钾浸渍在适当的载体上 如活性炭; 以及一种负载在多孔载体材料上的金属卤化物催化剂的再活化方法,包括干燥然后使负载的催化剂与卤化氢的气态物流接触一段时间,其足以将以任何形式存在的所有金属转化为相应的金属 卤化物。

    Catalyst regeneration method with three-zone combustion gas addition
    92.
    发明授权
    Catalyst regeneration method with three-zone combustion gas addition 失效
    添加三区燃烧气体的催化剂再生方法

    公开(公告)号:US5053371A

    公开(公告)日:1991-10-01

    申请号:US608518

    申请日:1990-11-02

    IPC分类号: B01J23/96 B01J38/44 C10G35/12

    摘要: A semi-continuous process for combusting coke from catalyst particles in a fixed bed is improved by injecting combustion air for the regeneration section to the three places, upper air to the burn zone, middle air to the chlorination zone and lower air to the burn zone. By this method combustion gas is added the halogenation gas loop which circulates chlorination gas around the chlorination zone in substantially closed system. Any gas that leaves the chlorination zone flows into the burn zone from the chlorination zone. Thus, passing additional air to the chlorination zone increases the oxygen concentration of the chloriation gas to that additional oxygen-containing chlorination gas and chlorination gas with a higher oxygen concentration passes into the burn zone from the chlorination zone. This method adds air for coke combustion and improves platinum dispersion in the halogenation zone.

    摘要翻译: 通过向三个地方注入用于再生段的燃烧空气,将上部空气喷射到燃烧区,中间空气到氯化区和降低空气到燃烧区,从而提高了在固定床中从催化剂颗粒燃烧焦炭的半连续方法 。 通过该方法,燃烧气体添加卤化气体回路,其在基本上封闭的系统中在氯化区周围循环氯化气体。 任何离开氯化区的气体从氯化区流入燃烧区。 因此,将额外的空气传递到氯化区使得氯化气体的氧浓度增加到附加的含氧氯化气体,并且具有较高氧浓度的氯化气体从氯化区进入燃烧区。 该方法为焦炭燃烧添加空气,并改善了卤化区中的铂分散。

    Apparatus for regeneration of hydrocarbon conversion catalyst
    93.
    发明授权
    Apparatus for regeneration of hydrocarbon conversion catalyst 失效
    烃转化催化剂再生装置

    公开(公告)号:US4832921A

    公开(公告)日:1989-05-23

    申请号:US920473

    申请日:1986-10-20

    摘要: A vessel for effecting multiple treatment steps needed to regenerate spent hydrocarbon conversion catalyst. Regeneration is accomplished in a moving bed of catalyst, where catalyst is passed through several treatment zones in the regeneration vessel. Catalyst is contacted with a hot oxygen-containing gas stream in order to remove coke which accumulates on the catalyst while it is in a hydrocarbon conversion zone. After the coke is burned off in a combustion zone, catalyst is passed into a drying zone for removal of water formed in the combustion zone which has remained on the catalyst instead of being carried off with combustion gases. Water removal is accomplished by passing a hot dry air stream through the catalyst. This air stream is introduced into the bottom of the regeneration vessel and is heated by exchange of heat with catalyst, thereby effecting the required cooling of the catalyst. Before passing into the drying zone, the air is heated further by heating element located in the vessel. After passing through the drying zone, the air stream provides oxygen for combustion in the combustion zone.

    摘要翻译: 用于进行多次处理步骤的容器用于再生废烃转化催化剂。 在催化剂的移动床中完成再生,其中催化剂通过再生容器中的若干处理区。 催化剂与含热氧气流接触,以便在碳氢化合物转化区中除去积聚在催化剂上的焦炭。 在焦炭在燃烧区中燃烧之后,将催化剂送入干燥区以除去在燃烧区中形成的水​​,该燃烧区中残留在催化剂上而不是被燃烧气体带走。 通过使热的干燥空气流通过催化剂来实现除水。 将该空气流引入再生容器的底部,并通过与催化剂的热交换进行加热,从而进行所需的催化剂冷却。 在进入干燥区之前,通过位于容器中的加热元件进一步加热空气。 在通过干燥区之后,空气流提供用于在燃烧区燃烧的氧气。

    Regeneration and reactivation of reforming catalysts while passivating
iron scale carryover from the regenerator circuit to the reactors
    94.
    发明授权
    Regeneration and reactivation of reforming catalysts while passivating iron scale carryover from the regenerator circuit to the reactors 失效
    重整催化剂的再生和再活化,同时使铁垢从蓄电池回路钝化到反应器

    公开(公告)号:US4738939A

    公开(公告)日:1988-04-19

    申请号:US67541

    申请日:1987-06-29

    申请人: Joseph P. Boyle

    发明人: Joseph P. Boyle

    CPC分类号: B01J38/44 B01J23/96 C10G35/09

    摘要: A process for the regeneration and reactivation of coked iridium-containing catalysts, and chemical modification and passivation of iron scale carried over from a ferrous metal regeneration circuit to the catalyst-containing reactor, or reactors, to suppress reaction between the iron scale and catalyst as normally occurs when iron scale contacts the catalyst of a reactor, or reactors. The iron scale is rendered non-reactive or inert in the reactor environment by converting the iron scale to a passive form, preferably ferric oxide, by employing ab initio an extended low temperature primary burn while purging the system of carbon oxides, notably carbon monoxide and carbon dioxide. Thereafter, the agglomerated metal, or metals, component of the catalyst is redispersed at conditions insufficient to reduce the oxidized iron scale which is contained in admixture with the regenerated catalyst. The agglomerated metal, or metals, component of the regenerated catalyst contained in admixture with the passivated iron scale is redispersed in a non-reducing atmosphere to return the catalyst to its active state without reduction of the passivated iron scale. This process is an improvement in those described in U.S. Pat. No. 4,514,284 and U.S. Pat. No. 4,517,076, respectively.

    Regeneration of hydrocarbon conversion catalyst
    95.
    发明授权
    Regeneration of hydrocarbon conversion catalyst 失效
    烃转化催化剂的再生

    公开(公告)号:US4647549A

    公开(公告)日:1987-03-03

    申请号:US814337

    申请日:1985-12-27

    摘要: A vessel for effecting multiple treatment steps needed to regenerate spent hydrocarbon conversion catalyst. Regeneration is accomplished by means of a moving bed of catalyst, where catalyst is passed through several treatment zones in the regeneration vessel. Catalyst is contacted with a hot oxygen-containing gas stream in order to remove coke which accumulates on the catalyst while it is in a hydrocarbon conversion zone. After the coke is burned off in a combustion zone, catalyst is passed into a drying zone for removal of water formed in the combustion zone which has remained on the catalyst instead of being carried off with combustion gases. Water removal is accomplished by passing a hot dry air stream through the catalyst. This air stream is introduced into the bottom of the regeneration vessel and is heated by exchange of heat with catalyst, thereby effecting the required cooling of the catalyst. Before passing into the drying zone, the air is heated further by heating means located in the vessel. After passing through the drying zone, the air stream provides oxygen for combustion in the combustion zone.

    摘要翻译: 用于进行多次处理步骤的容器用于再生废烃转化催化剂。 通过催化剂的移动床实现再生,其中催化剂通过再生容器中的若干处理区。 催化剂与含热氧气流接触,以便在碳氢化合物转化区中除去积聚在催化剂上的焦炭。 在焦炭在燃烧区中燃烧之后,将催化剂送入干燥区以除去在燃烧区中形成的水​​,该燃烧区中残留在催化剂上而不是被燃烧气体带走。 通过使热的干燥空气流通过催化剂来实现除水。 将该空气流引入再生容器的底部,并通过与催化剂的热交换进行加热,从而进行所需的催化剂冷却。 在进入干燥区之前,通过位于容器中的加热装置进一步加热空气。 在通过干燥区之后,空气流提供用于在燃烧区燃烧的氧气。

    Regeneration of noble metal-highly siliceous zeolite with sequential
hydrogen halide and halogen or organic-halogen compound treatment
    96.
    发明授权
    Regeneration of noble metal-highly siliceous zeolite with sequential hydrogen halide and halogen or organic-halogen compound treatment 失效
    用连续卤化氢和卤素或有机 - 卤素化合物处理再生贵金属 - 高硅质沸石

    公开(公告)号:US4645751A

    公开(公告)日:1987-02-24

    申请号:US814082

    申请日:1985-12-23

    CPC分类号: B01J29/90 B01J38/44

    摘要: A process is described for rejuvenation of a deactivated highly siliceous noble metal-containing zeolite catalyst which contains agglomerated noble metals. The process comprises initially reducing the deactivated catalyst in hydrogen, pretreating the thus reduced catalyst with an inert gas stream containing about 0.001 to 10 weight percent hydrogen chloride, redispersing the noble metal with an inert gas stream containing about 0.001 to 10 weight percent Cl in the form of Cl.sub.2 or Cl-containing organic material, and subsequently reducing the catalyst. The Cl-treatments may optionally occur in the presence of oxygen or sources of oxygen.

    摘要翻译: 描述了一种包含聚集的贵金属的失活的高含硅含贵金属的沸石催化剂的再生方法。 该方法包括首先在氢中还原失活的催化剂,用含有约0.001至10重量%氯化氢的惰性气流预处理如此还原的催化剂,将贵金属用含有约0.001至10重量%Cl的惰性气流再分散在 形式的Cl 2或Cl的有机材料,随后还原催化剂。 Cl处理可以任选地在氧气或氧源存在下进行。

    Regeneration method for gravity-flowing deactivated catalyst particles
    98.
    发明授权
    Regeneration method for gravity-flowing deactivated catalyst particles 失效
    重力流失活催化剂颗粒的再生方法

    公开(公告)号:US4094814A

    公开(公告)日:1978-06-13

    申请号:US806885

    申请日:1977-06-15

    摘要: A continuous method for regenerating deactivated catalyst particles in a regeneration zone through which the particles are downwardly movable by way of gravity-flow. Particles are initially introduced into an upper carbon-burning/halogenation zone wherein they are contacted, in a first section, with a first air stream and a first mixture of steam and a halogen, or halogen-containing compound. Partially regenerated/reconditioned particles are then contacted, in a lower second section, with a second air stream and second mixture of steam and halogen. From this two-sectioned, carbon-burning/halogenation zone, the catalyst particles flow via gravity into a drying zone wherein they are contacted by a substantially dry air stream.

    摘要翻译: 用于在再生区再生失活的催化剂颗粒的连续方法,通过该再生区域,颗粒可以通过重力流向下移动。 颗粒最初被引入上碳燃烧/卤化区,其中它们在第一部分中与第一空气流和蒸汽和卤素或含卤素化合物的第一混合物接触。 然后,部分再生/再生的颗粒在较低的第二段中与第二空气流和蒸汽和卤素的第二混合物接触。 从这个两段式的碳燃烧/卤化区,催化剂颗粒通过重力流动到干燥区域,在这里干燥区域与基本上干燥的气流接触。

    Process for reactivation of iridium-containing catalysts
    99.
    发明授权
    Process for reactivation of iridium-containing catalysts 失效
    含铱催化剂再活化方法

    公开(公告)号:US3941716A

    公开(公告)日:1976-03-02

    申请号:US388908

    申请日:1973-08-16

    申请人: John D. Paynter

    发明人: John D. Paynter

    摘要: In a process for redispersion of the iridium agglomerates (irridium and/or iridium oxide) of a deactivated iridium-containing catalyst, especially a platinum-iridium catalyst, in ferrous metal equipment, wherein the agglomerated iridium, or agglomerated platinum and iridium, is redispersed and the catalyst reactivated by sequential prereduction-halogen treatments, the improvement comprising adding and maintaining small amounts of water with the halogen to suppress ferrous metal corrosion and catalyst contamination during the required treatment with halogen.

    摘要翻译: 在黑色金属设备中,将含有失活的含铱催化剂,特别是铂 - 铱催化剂的铱团聚体(铱和/或氧化铱)再分散的方法,其中附聚的铱或附聚的铂和铱被再分散 并且催化剂通过连续预还原卤素处理再活化,改进包括在卤素所需处理期间用卤素添加和维持少量的水以抑制黑色金属腐蚀和催化剂污染。

    Regeneration of a coke-deactivated catalyst comprising a combination of platinum,tin and halogen with a porous carrier material
    100.
    发明授权
    Regeneration of a coke-deactivated catalyst comprising a combination of platinum,tin and halogen with a porous carrier material 失效
    含有多孔载体材料的包含铂,钛和卤素组合的焦炭活化催化剂的再生

    公开(公告)号:US3803052A

    公开(公告)日:1974-04-09

    申请号:US22631772

    申请日:1972-02-14

    发明人: HAYES J

    摘要: A deactivated hydrocarbon conversion catalyst, which is a combination of catalytically effective amounts of a platinum group component, a tin component and a halogen component with a porous carrier material, which is free of labile sulfur and which has been deactivated by a deposition of carbonaceous material thereon during a previous contacting with a hydrocarbon charge stock at hydrocarbon conversion conditions, is regenerated by the sequential steps of: (1) burning carbon from the deactivated catalyst at a relatively low temperature with a substantially sulfur-free first gaseous mixture containing relatively small amounts of oxygen, H2O and HCl; (2) treating the resulting catalyst at a relatively high temperature with a second gaseous mixture containing O2, H2O and HCl; (3) purging oxygen from contact with the resulting catalyst; and (4) reducing the resulting catalyst by contacting with a substantially sulfur-free third gaseous mixture containing hydrogen and small amounts of H2O and HCl. Key features of the regeneration method involve: the presence of both H2O and HCl in the gaseous mixtures used in the carbon-burning, oxygen-treating and reduction steps; the use of sulfur-free gaseous mixtures in all of these steps; and the careful control of the mole ratio of H2O to HCl employed in each of these gaseous mixtures.