Combination reforming process
    1.
    发明授权
    Combination reforming process 失效
    组合改造工艺

    公开(公告)号:US3791961A

    公开(公告)日:1974-02-12

    申请号:US3791961D

    申请日:1971-12-07

    Inventor: SINFELT J

    CPC classification number: C10G59/02 B01J23/468 B01J37/22 C10G35/09

    Abstract: A CONVENTIONAL NAPHTHENE DEHYDROGENATION CATALYST, SUCH AS A PLATINUM-HALOGEN-ALUMINA CATALYST, IS USED IN THE INITIAL ZONE OR REACTORS IN A CATALYTIC REFORMING PROCESS; THE TAIL ZONE OR REACTORS CONTAINS A SUPPORTED GROUP VIII POLYMETALLIC CATALYST WITH PLATINUM AS ONE OF THE METALLIC COMPONENTS. IN A PREFERRED EMBODIMENT, THE TAIL ZONE CONTAINS A PLATINUM-IRIDIUM CATALYST ONE A POROUS SUPPORT SUCH AS ALUMINA. IN THE TAIL REACTORS, CONVERSION OF PARAFFINS IS OF PRIMARY IMPORTANCE, ALONG WITH DEALKYLATION OF ALKYLBENEZENES; IN THE INITIAL REACTORS, THE PREDOMINANT REACTION IS THE CONVERSION OF NAPHTTHENES TO AROMATICS. THE COMBINATION PROCESS RESULTS IN THE FORMATION OF A SIGNIFICANTLY GREATER OCTANE NUMBER PRODUCT THAN IS OBTAINED IN A CONVENTIONAL REOFMING PROCESS IN WHICH PLATINUM-ALUMINA CATALYST IS USED THROUGHOUT.

    Method for preparation of catalysts
    2.
    发明授权
    Method for preparation of catalysts 失效
    催化剂的制备方法

    公开(公告)号:US3789020A

    公开(公告)日:1974-01-29

    申请号:US3789020D

    申请日:1971-02-01

    Inventor: CARTER J SINFELT J

    CPC classification number: C10G35/09 B01J23/656 B01J23/89 C10G35/095

    Abstract: A METHOD OF THE PREPARATION OF A CATALYST COMPRISING THE SEQUESTRATION OF MICRONUTRIENT METAL IONS IN LIQUID TWO OR MORE METALS IN LOW CONCENTRATION OND ONE OR MORE PHOSPHATIC FERTILIZER SOLUTIONS IS FACILITATED BY INCORPORATING I NONMETALLIC REFRACTORY MATERIALS IN HIGH CONCENTRATIONS N WHICH COMPRISES SUPPORTING THE METALS ON A FRACTION OF THE SOLUTIONS A SYNERGISTIC COMBINATION OF CITRATE AND THE NONMETALLIC REFRACTORY MATERIAL, AND MIXING SAID FRACPOLYPHOSPHATE SALTS. TION WITH THE REMAINING NONMETALLIC REFRACTORY MATERIAL, WHEREBY THE OVERALL CATALYST AT REACTION CONDUCTIONS CONSISTS OF A PHYSICAL MIXTURE OF THE SUPPORTED METALLIC COMPONENT AND THE REMAINING NONOMETALLIC REFRACTORY MATERIAL. MORE PARTICULARLY, THE SUPPORTED METALLIC COMPONENT IS TREATED UNDER REDUCING CONDITIONS TO FORM AN ALLOY OF THE MATALS ON SAID FRACTION ON THE NONMETALLIC REFRACTORY MATERIAL. IN PREFFERED EMBODIMENTS THE SUPPORTED METALLIC COMPONENT OF THE CATALYST COMPRISES TWO METALS, ONE FROM GROUP VIII AND ONE FROM GROUP I-B. OR BOTH FROM GROUP VIII.

    High severity reforming process with a platinum-iridium catalyst
    3.
    发明授权
    High severity reforming process with a platinum-iridium catalyst 失效
    具有铂 - 铱催化剂的高严重性改性方法

    公开(公告)号:US3839194A

    公开(公告)日:1974-10-01

    申请号:US35040373

    申请日:1973-04-12

    Inventor: SINFELT J BARNETT A

    Abstract: Naphtha feed stocks are converted to high octane products in a long cycle semi-regenerative operation utilizing a catalyst comprising alumina in association with 0.15 to 0.75 weight percent platinum, 0.15 to 0.45 weight percent iridium and 0.3 to 2.0 weight percent chlorine, each based on total catalyst, the surface area of the platinum and iridium on the alumina being at least about 200 square meters per gram of platinum and iridium as determined by carbon monoxide chemisorption techniques. The catalyst should contain less than about two atoms of sulfur per atom of platinum and iridium and be substantially free of alkali and alkaline earth metal constituents.

    Abstract translation: 石油醚原料在长循环半再生操作中转化为高辛烷值产物,利用包含氧化铝的催化剂与0.15至0.75重量%的铂,0.15至0.45重量百分比的铱和0.3至2.0重量百分比的氯,基于总计 催化剂中,铂和铱在氧化铝上的表面积为至少约200平方米/克铂和铱,通过一氧化碳化学吸附技术测定。 催化剂应含有少于约两个原子的硫原子的铂和铱,并且基本上不含碱金属和碱土金属成分。

    Hydrocarbon conversion using an iridium-gold catalyst
    4.
    发明授权
    Hydrocarbon conversion using an iridium-gold catalyst 失效
    使用红色金属催化剂进行烃转化

    公开(公告)号:US3850747A

    公开(公告)日:1974-11-26

    申请号:US19446171

    申请日:1971-11-01

    Inventor: SINFELT J BARNETT A

    Abstract: Hydrocarbon materials are converted to useful products by contacting the same at elevated temperatures with a catalyst comprising a refractory support in association with greater than 0.1 wt. % iridium, and 0.1 - 1.0 wt. % of at least one additional metal. The iridium and additional catalyst metal, preferably platinum, are present on the surface of the support in the form of highly dispersed polymetallic clusters with metal surface areas of at least 200 square meters per gram of metal. The catalyst is particularly effective for promoting naphtha reforming operations.

    Abstract translation: 碳氢化合物材料通过在升高的温度下与含有大于0.1重量%的耐火载体的催化剂接触而转化为有用的产物。 %铱,和0.1〜1.0wt。 至少一种额外金属的%。 铱和另外的催化剂金属(优选铂)以高度分散的多金属簇的形式存在于载体的表面上,金属表面积为至少200平方米/克金属。 催化剂对于促进石脑油重整操作特别有效。

    Catalytic reforming process
    7.
    发明授权
    Catalytic reforming process 失效
    催化重整工艺

    公开(公告)号:US3729408A

    公开(公告)日:1973-04-24

    申请号:US3729408D

    申请日:1970-12-28

    Inventor: CARTER J SINFELT J

    Abstract: A catalytic reforming process wherein naphtha feed streams, boiling from about 80* to 450* F, and comprising naphthenes, paraffins and aromatics, are contacted, in an initial reaction zone, with a hydrogen containing gas, in the presence of a catalyst comprising Pt and a group IB metal supported on a refractory oxide; passed into a tail zone wherein the feed stream is again contacted with a catalyst and thereby further reacted; and a high octane product is recovered. In a preferred embodiment the Group IB metal is Cu.

    Abstract translation: 在催化重整过程中,在初始反应区中,在含有Pt的催化剂存在下,将沸点为约80-450°F的石脑油进料流,包含环烷烃,链烷烃和芳族化合物与含氢气体接触, 和负载在难熔氧化物上的IB族金属; 进入尾区,其中进料流再次与催化剂接触,从而进一步反应; 并回收高辛烷值的产品。 在优选实施方案中,IB族金属是Cu。

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