Process for the production of ether and alcohol
    1.
    发明授权
    Process for the production of ether and alcohol 失效
    醚和酒精生产工艺

    公开(公告)号:US4857664A

    公开(公告)日:1989-08-15

    申请号:US265324

    申请日:1988-10-27

    IPC分类号: C07C41/06 C07C41/09 C07C41/42

    CPC分类号: C07C41/42 C07C41/06 C07C41/09

    摘要: Olefin undergoes conversion in the presence of water to a mixture of alcohol and ether which is then subjected to various downstream operations including distillation and decantation to provide an ether-rich product containing little if any water. If desired the ether can be combined in any predetermined ratio with co-produced alcohol to provide alcohol/ether mixtures of desired composition. The foregoing process is especially suitable to the conversion of propylene and propylene-containing streams to diisopropyl ether and mixtures of isopropyl alcohol and diisopropyl ether which are useful, inter alia, as octane improves for gasoline.

    摘要翻译: 烯烃在水的存在下经历转化为醇和醚的混合物,然后将其进行各种下游操作,包括蒸馏和倾析,以提供含有少量的含有醚的产物。 如果需要,醚可以以任何预定比例与共同产生的醇组合以提供所需组合物的醇/醚混合物。 上述方法特别适用于将丙烯和含丙烯的物流转化为二异丙基醚以及异丙醇和二异丙醚的混合物,特别是对于汽油而言辛烷值改善。

    Lubricant production process
    3.
    发明授权
    Lubricant production process 失效
    润滑油生产过程

    公开(公告)号:US4919788A

    公开(公告)日:1990-04-24

    申请号:US260857

    申请日:1988-10-21

    IPC分类号: C10G45/64 C10G65/04 C10G67/04

    摘要: A process for producing lubricant oils of low pour point and high viscosity index by first carrying out a partial dewaxing of a lubricant base stock in an initial catalytic dewaxing operation, followed by a selective dewaxing step. The initial catalytic dewaxing step is carried out using a large pore, high silica zeolite dewaxing catalyst such as high silica Y or zeolite beta which dewaxes by isomerizing the waxy components of the base stock to less waxy brance chain isoparaffins but the severity of the operation is controlled so as to effect only a partial removal of the waxy components. Further removal of the waxy components is effected during the subsequent dewaxing step which is selective for the removal of the more waxy n-paraffin components, leaving the branched chain isoparaffins which contribute to a high VI in the product. The selective dewaxing step may be either a solvent, e.g. MEK dewaxing operation or a catalytic dewaxing using a highly shape selective zeolite such as ZSM-22 or ZSM-23. The severity of the initial catalytic dewaxing operation may be controlled so as to effect a net increase in the content of isoparaffins and because of the selective nature of the solvent dewaxing step, this increased isoparaffins concentration may be retained, producing a product of high VI. The pour point of the feedstock is preferably reduced during the initial catalytic dewaxing step to a value which is no lower than 10.degree. F. and preferably no lower than 20.degree. F., above the target pour point for the products. Generally, this will entail a reduction of at least 10.degree. F. and preferably at least 20.degree. F. in the pour point of the feed.

    摘要翻译: 首先在初始催化脱蜡操作中进行润滑剂原料的部分脱蜡,然后进行选择性脱蜡步骤,生产低倾点和高粘度指数的润滑油的方法。 初始催化脱蜡步骤使用大孔,高二氧化硅沸石脱蜡催化剂如高二氧化硅Y或沸石β进行,该脱蜡通过使基础油料的蜡质组分异构化成较少的蜡状分支链异链烷烃,但操作的严重性是 被控制以仅影响蜡组分的部分去除。 在随后的脱蜡步骤中进一步除去蜡状组分,该脱蜡步骤选择性地除去更多的蜡状正链烷烃组分,留下有助于产物中高VI的支链异链烷烃。 选择性脱蜡步骤可以是溶剂,例如 MEK脱蜡操作或使用ZSM-22或ZSM-23等高选择性沸石的催化脱蜡。 可以控制初始催化脱蜡操作的严重性,以便实现异链烷烃含量的净增加,并且由于溶剂脱蜡步骤的选择性,可以保留这种增加的异链烷烃浓度,从而产生高VI的产物。 原料的倾点优选在初始催化脱蜡步骤期间降低至不低于产物的目标倾点的10°F,优选不低于20°F的值。 通常,这将导致在进料的倾点下降至少10°F,优选至少降低20°F。

    Process for producing alkyl aromatic compounds
    4.
    发明授权
    Process for producing alkyl aromatic compounds 失效
    烷基芳族化合物的制备方法

    公开(公告)号:US4409412A

    公开(公告)日:1983-10-11

    申请号:US423337

    申请日:1982-09-24

    IPC分类号: C07C2/86

    摘要: A process for alkylating aromatic compounds wherein the product aromatics are provided with one or more alkyl groups possessing at least two carbon atoms is disclosed wherein starting aromatic compound(s) and an alkylating atent which is a mixture of hydrogen and/or a hydrogen-containing substance which provides hydrogen under process conditions and a carbon oxide, e.g., a mixture of syngas (hydrogen and carbon monoxide) are reacted at elevated temperature in the presence of an activated catalyst containing metal values selected from the group consisting of iron, cobalt, ruthenium, manganese, rhodium and osmium, and a zeolite having a constraint index of 12 or less, e.g., ZSM-5. The alkylated aromatics can be dealkylated by known and conventional means to provide olefin and the dealkylated aromatics can be recycled to the alkylation zone.

    摘要翻译: 公开了一种芳族化合物的烷基化方法,其中产物芳族化合物具有一个或多个具有至少两个碳原子的烷基,其中起始芳族化合物和烷基化剂是氢和/或含氢的混合物 在工艺条件下提供氢的物质和碳氧化物,例如合成气(氢气和一氧化碳)的混合物在升高的温度下在活性催化剂存在下反应,所述催化剂含有选自铁,钴,钌的金属值 ,锰,铑和锇以及具有12或更小约束指数的沸石,例如ZSM-5。 烷基化芳族化合物可以通过已知和常规方法脱烷基化以提供烯烃,并且脱烷基化的芳族化合物可以再循环到烷基化区。

    Redispersion of noble metal on low acidity support
    5.
    发明授权
    Redispersion of noble metal on low acidity support 失效
    贵金属在低酸性载体上的再分散

    公开(公告)号:US5188996A

    公开(公告)日:1993-02-23

    申请号:US704152

    申请日:1991-05-22

    IPC分类号: B01J23/96 B01J38/44

    CPC分类号: B01J38/44 B01J23/96

    摘要: A process is described for redispersing agglomerated metal on a catalyst. The catalyst comprises noble metal on a low acidity oxide support, and the process comprises contacting the catalyst with a gas stream containing about 3 to about 6 Torr chlorine and about 250 to about 750 Torr oxygen under conditions sufficient to achieve redispersion.

    摘要翻译: 描述了一种将附聚的金属重新分散在催化剂上的方法。 该催化剂包含在低酸性氧化物载体上的贵金属,并且该方法包括在足以实现再分散的条件下使催化剂与含有约3至约6托氯和约250至约750托氧的气流接触。

    Dual function catalyst and isomerization therewith
    6.
    发明授权
    Dual function catalyst and isomerization therewith 失效
    双功能催化剂及其异构化

    公开(公告)号:US5028573A

    公开(公告)日:1991-07-02

    申请号:US471462

    申请日:1990-01-29

    CPC分类号: B01J29/40 C07C5/2724

    摘要: A dual function composite catalyst for isomerizing an isomerization feed containing an aromatic C.sub.8 mixture of ethyl benzene and xylene, comprises (a) a crystalline aluminosilicate zeolite having a low acid activity as measured by an alpha value of from 0.02 to 11, an average crystal size of not more than 0.4 microns for at least 50% by weight of the crystals, a silica to alumina ratio of at least about 12, a constraint index of about 1 to 12, a xylene sorption capacity greater than 1 gram per 100 grams of zeolite, and an ortho-xylene sorption time for 30 percent of said capacity less than 10 minutes, said sorption capacity and sorption time being measured at 120.degree. C. and a xylene pressure of 4.5.+-.0.8 mm of mercury, and (b) a supported metal of Group VIII of the Periodic Table having a high hydrogenation/dehydrogenation activity to provide the catalyst with a dehydrogenation activity of at least 10. The catalyst has an alpha value of 0.005 to 3.

    摘要翻译: 用于异构化异构化进料的双功能复合催化剂,其含有乙苯和二甲苯的芳族C 8混合物,包括(a)具有低酸活性的结晶硅铝酸盐沸石,其α值为0.02至11,平均晶体尺寸 对于至少50重量%的晶体,二氧化硅与氧化铝的比例至少约为12,约1到12的约束指数,每100克沸石的二甲苯吸附容量大于1克,不超过0.4微米 ,并且邻二甲苯吸附时间为所述容量的30%小于10分钟,所述吸附容量和吸附时间在120℃下测量,二甲苯压力为4.5 +/- 0.8mm汞柱,(b) 元素周期表第VIII族的负载金属具有高的氢化/脱氢活性,以使催化剂具有至少10的脱氢活性。该催化剂具有0.005至3的α值。

    Redispersion of agglomerated noble metals on zeolite catalysts
    7.
    发明授权
    Redispersion of agglomerated noble metals on zeolite catalysts 失效
    附聚贵金属在沸石催化剂上的再分散

    公开(公告)号:US4657874A

    公开(公告)日:1987-04-14

    申请号:US819074

    申请日:1986-01-15

    摘要: A process is described for rejuvenation of a deactivated highly siliceous noble metal-containing zeolite catalyst having a framework silica to alumina ratio of at least about 20 which contains agglomerated noble metal in its deactivated state. The process comprises redispersing the noble metals associated with the deactivated catalyst by contacting the catalyst with a stream of inert gas containing molecular chlorine, water and optionally, oxygen, a temperatures ranging from about 150.degree. to about 450.degree. C., a partial pressure of chlorine of from about 6 to about 15 Torr and a ratio of partial pressure of water to partial pressure of chlorine of from about 0.01 to about 2 for a period of time sufficient to achieve redispersion; purging said catalyst with an inert gas; and reducing said purged catalyst in a stream of hydrogen at a temperature ranging from about 140.degree. C. to 550.degree. C.

    摘要翻译: 描述了一种用于使具有至少约20的骨架二氧化硅与氧化铝比的失活的高含硅含贵金属的沸石催化剂再生的方法,其含有处于其失活状态的附聚的贵金属。 该方法包括通过使催化剂与含有分子氯,水和任选的氧的惰性气体流接触来将与失活的催化剂相关联的贵金属再分散,温度范围为约150℃至约450℃, 约6至约15托的氯,水的分压与氯的分压的比例为约0.01至约2,持续足以实现再分散的时间; 用惰性气体吹扫所述催化剂; 并在约140℃至550℃的温度范围内将氢气流中的所述吹扫的催化剂还原。

    Conversion of ketones over metal-containing zeolite catalysts
    8.
    发明授权
    Conversion of ketones over metal-containing zeolite catalysts 失效
    酮与含金属的沸石催化剂的转化

    公开(公告)号:US4339606A

    公开(公告)日:1982-07-13

    申请号:US232074

    申请日:1981-02-06

    IPC分类号: C07C45/73 C07C45/45

    CPC分类号: C07C45/73

    摘要: Ketones are converted in one step to saturated dimeric ketones by passing them over a zeolite having a silica to alumina ratio of at least 12 and a Constraint Index of from 1 to 12 and containing a Group VIII metal.

    摘要翻译: 将酮通过使它们通过二氧化硅与氧化铝之比至少为12且约束指数为1至12并含有第Ⅷ族金属的沸石而在一个步骤中转化成饱和二聚酮。

    Conversion of synthesis gas to hydrocarbon mixtures
    9.
    发明授权
    Conversion of synthesis gas to hydrocarbon mixtures 失效
    将合成气转化为烃混合物

    公开(公告)号:US4157338A

    公开(公告)日:1979-06-05

    申请号:US883970

    申请日:1978-03-06

    IPC分类号: C07C1/04

    CPC分类号: C07C1/0455 C07C2529/068

    摘要: A mixture of carbon monoxide and hydrogen is contacted with a mixture comprising an element selected from the group consisting of ruthenium, rhodium and osmium carbon monoxide reduction catalyst and a crystalline alumino-silicate providing a pore dimension greater than about 5 Angstroms and a constraint index in the range of 1 to 12 to produce hydrocarbon mixtures useful in forming gasoline boiling range products, aromatic rich hydrocarbons, and chemical intermediates.

    摘要翻译: 将一氧化碳和氢气的混合物与包含选自钌,铑和锇一氧化碳还原催化剂的元素的混合物和提供孔尺寸大于约5埃的结晶铝硅酸盐接触,并且约束指数 范围为1至12,以产生可用于形成汽油沸点产物,富含芳烃的化学中间体的烃混合物。

    Process for producing diesel fuel with increased cetane number
    10.
    发明授权
    Process for producing diesel fuel with increased cetane number 有权
    生产柴油增加十六烷值的方法

    公开(公告)号:US06210563B1

    公开(公告)日:2001-04-03

    申请号:US09222977

    申请日:1998-12-30

    IPC分类号: C10G35085

    CPC分类号: C10G45/54 C10G2400/04

    摘要: A process is provided for selectively producing diesel fuel with increased cetane number from a hydrocarbon feedstock. The process includes contacting the feedstock with a catalyst which has a large pore crystalline molecular sieve material component having a faujasite structure and alpha acidity of less than 1, preferably about 0.3 or less. The catalyst also contains a dispersed Group VIII noble metal component which catalyzes the hydrogenation/hydrocracking of the aromatic and naphthenic species in the feedstock.

    摘要翻译: 提供了一种从碳氢化合物原料选择性地生产具有增加的十六烷值的柴油燃料的方法。 该方法包括使原料与催化剂接触,所述催化剂具有大孔分子筛材料组分,其具有八面沸石结构和α酸度小于1,优选约0.3或更小。 催化剂还含有分散的VIII族贵金属组分,其催化原料中芳族和环烷烃物质的氢化/加氢裂化。