Isopropyl alcohol and diispropyl ether production from crude by-product
acetone in one step
    5.
    发明授权
    Isopropyl alcohol and diispropyl ether production from crude by-product acetone in one step 失效
    异丙醇和二异丙醚由粗副产物丙酮一步法生产

    公开(公告)号:US5637778A

    公开(公告)日:1997-06-10

    申请号:US287451

    申请日:1994-08-08

    CPC classification number: C07C41/09 C07C29/145 C07C41/01

    Abstract: Disclosed is a one-step method for synthesis of methyl tertiary butyl ether, diisopropyl ether and isopropyl ether from crude streams containing acetone, methanol and t-butyl alcohol which comprises reacting an acetone-rich feed over a bifunctional catalyst comprising 5-45% by weight of a catalyst consisting essentially of a hydrogenation catalyst selected from the group consisting of one or more metals selected from the group consisting of IB, VIB or VIII of the Periodic Table and a heteropoly acid on a 55%-95% of the total weight of the catalyst of a support comprising a compound selected from the group consisting of:a. a metal phosphate;b. 5 to 95% by weight metal phosphate supported on 95 to 5 wt % Group III or IV oxide; andc. a large pore silicoaluminophosphate.

    Abstract translation: 公开了一种从含有丙酮,甲醇和叔丁醇的原料流合成甲基叔丁基醚,二异丙基醚和异丙醚的一步法,该方法包括使富含丙酮的原料在双功能催化剂上反应,所述双功能催化剂包含5-45% 基本上由选自由周期表的IB,VIB或VIII中的一种或多种金属组成的组中的氢化催化剂和总重量的55%-95%的杂多酸组成的催化剂的重量 的包含选自以下的化合物的载体的催化剂:a。 金属磷酸盐; b。 负载在95至5重量%III或IV族氧化物上的5至95重量%的金属磷酸盐; 和c。 大孔硅铝磷酸盐。

    Integrated process for the production of isopropyl alcohol and
diisopropyl ethers
    6.
    发明授权
    Integrated process for the production of isopropyl alcohol and diisopropyl ethers 失效
    用于生产异丙醇和二异丙醚的综合方法

    公开(公告)号:US5583266A

    公开(公告)日:1996-12-10

    申请号:US236807

    申请日:1994-05-02

    CPC classification number: C07C29/141 C07C41/09 Y02P20/125

    Abstract: A two-step integrated process for the generation of diisopropyl ether from a crude by-product acetone stream which comprises:a) Hydrogenating said crude acetone over a supported, hydrogenation catalyst to give an isopropanol-rich effluent;b) passing said isopropanol-rich intermediate directly to a second reactor, andc) subject said IPA to dehydration conditions in the presence of hydrogen and a strong acid zeolite catalyst from the group consisting of .beta.-zeolite, optionally modified with one or more metals from Groups IB, VIB, VIIB and VIII of the Periodic Table, and a dealuminized Y-zeolite.

    Abstract translation: 一种用于从粗副产物丙酮流产生二异丙醚的两步整合方法,其包括:a)在负载的氢化催化剂上氢化所述粗丙酮,得到富含异丙醇的流出物; b)将富含异丙醇的中间体直接通入第二反应器,以及c)使所述IPA在氢气和强酸沸石催化剂存在下脱水条件,所述沸石催化剂由β-沸石组成,所述β-沸石任选用一种或多种金属 来自元素周期表的IB,VIB,VIIB和VIII族,脱铝的Y-沸石。

    Catalytic process for dewaxing hydrocarbon feedstocks
    7.
    发明授权
    Catalytic process for dewaxing hydrocarbon feedstocks 失效
    用于脱蜡烃原料的催化方法

    公开(公告)号:US5332490A

    公开(公告)日:1994-07-26

    申请号:US952037

    申请日:1992-09-28

    CPC classification number: C10G45/64 C10G2400/10

    Abstract: A process for hydrodewaxing a hydrocarbon feedstock boiling above about 350.degree. F. by contacting the feedstock and hydrogen at a hydrogen pressure of from about 300 to about 2000 psig at a temperature of 400.degree. to 900.degree. F. and at a space velocity of about 0.1 to about 10.0 LHSV with a catalyst comprising about 0.1 to about 23 wt. % of an oxide of a Group VIII metal, such as nickel, or an oxide of a Group VIB metal, such as molybdenum; supported on a porous alumina support containing about 50 to about 85 wt. % of a crystalline alumino-silicate zeolite of the ZSM-5 type based on the weight of the support. The catalyst is further characterized by having greater than 60% of the pore volume between 45-600 Angstroms in the 70-200 Angstrom range. The process is especially useful for dewaxing lubricating oil basestocks.

    Abstract translation: 通过使原料和氢气在约300至约2000psig的氢气压力下在400-900°F的温度和大约的空间速度下接触原料和氢气,将沸点高于约350°F的烃原料加氢脱蜡的方法。 0.1至约10.0LHSV,催化剂包含约0.1至约23重量% %的Ⅷ族金属的氧化物,例如镍,或ⅥB族金属的氧化物如钼; 负载在含有约50至约85重量%的多孔氧化铝载体上。 %的基于载体重量的ZSM-5型结晶铝硅酸盐沸石。 该催化剂的特征还在于在70-200埃范围内具有大于60%的孔体积在45-600埃之间。 该方法对于脱蜡润滑油基础油料特别有用。

Patent Agency Ranking