Thermal cracking of heavy fraction of hydrocarbon hydrogenate
    1.
    发明授权
    Thermal cracking of heavy fraction of hydrocarbon hydrogenate 失效
    重质烃氢化物的热裂解

    公开(公告)号:US4310409A

    公开(公告)日:1982-01-12

    申请号:US197377

    申请日:1980-10-16

    CPC classification number: C10G69/06 C10G2400/20

    Abstract: To obtain olefins by the thermal cracking of hydrocarbons, e.g., vacuum gas oil, by hydrogenation and subsequent steam cracking, an intermediate fractionation of the hydrogenate is provided so that the light fraction enriched in branched isomers can be used as fuel and the heavy fraction only is subjected to the steam cracking.

    Abstract translation: 为了通过烃的热裂解(例如真空瓦斯油)通过氢化和随后的蒸汽裂解来获得烯烃,提供氢化物的中间分馏,使得富含支化异构体的轻馏分可以用作燃料,仅用于重馏分 受到蒸汽破裂的影响。

    Unsupported catalysts in the production of olefins
    2.
    发明授权
    Unsupported catalysts in the production of olefins 失效
    不饱和的催化剂生产烯烃

    公开(公告)号:US4210520A

    公开(公告)日:1980-07-01

    申请号:US905485

    申请日:1978-05-12

    CPC classification number: C10G45/46 C10G2400/06 C10G2400/20

    Abstract: In a process for the production of olefins in two stages wherein, in the first stage, heavy petroleum fractions are hydrogenated in the presence of hydrogen and a hydrogenation catalyst and, in the second stage, the thus-hydrogenated fractions are subjected to thermal cracking in the presence of steam, the improvement which comprises employing as the hydrogenation catalyst a support-free catalyst consisting essentially of elements from Groups VIb, VIIB, and VIII of the periodic table of the elements in the form of the metals, metal oxides, metal sulfides, or organometal complexes, or mixtures thereof.

    Abstract translation: 在二阶段生产烯烃的方法中,其中在第一阶段中,在氢气和氢化催化剂存在下将重质石油馏分氢化,并且在第二阶段中将如此氢化的馏分在 蒸汽的存在,其改进包括使用作为氢化催化剂的无载体催化剂,其基本上由金属,金属氧化物,金属硫化物形式的元素周期表第VIb,VIIB和VIII族元素组成 ,或有机金属配合物,或其混合物。

    Thermal cracking of heavy fraction of hydrocarbon hydrogenate
    3.
    发明授权
    Thermal cracking of heavy fraction of hydrocarbon hydrogenate 失效
    重质烃氢化物的热裂解

    公开(公告)号:US4260474A

    公开(公告)日:1981-04-07

    申请号:US82453

    申请日:1979-10-09

    CPC classification number: C10G69/06 C10G2400/20

    Abstract: To obtain olefins by the thermal cracking of hydrocarbons, e.g., vacuum gas oil, by hydrogenation and subsequent steam cracking, an intermediate fractionation of the hydrogenate is provided so that the light fraction enriched in branched isomers can be used as fuel and the heavy fraction only is subjected to the steam cracking.

    Abstract translation: 为了通过烃的热裂解(例如真空瓦斯油)通过氢化和随后的蒸汽裂解来获得烯烃,提供氢化物的中间分馏,使得富含支化异构体的轻馏分可以用作燃料,仅用于重馏分 受到蒸汽破裂的影响。

    Catalyst for decreasing the content of nitrogen oxides in flue gases
    5.
    发明授权
    Catalyst for decreasing the content of nitrogen oxides in flue gases 失效
    用于降低烟道气中氮氧化物含量的催化剂

    公开(公告)号:US4734391A

    公开(公告)日:1988-03-29

    申请号:US895559

    申请日:1986-08-11

    CPC classification number: B01J21/16 B01D53/8628

    Abstract: A catalyst for decreasing the content of nitrogen oxides in flue gases. The catalyst contains at least one of the metals titanium, zirconium, vanadium, tungsten, molybdenum, or cerium in the form of one or more of their oxides combined with a silicate with a three-layer structure (three-layer silicate) selected from the group consisting of illite and mica. The atomic ratio of the silicon in the three-layer silicate to the metal in the oxide is from 0.2 and 50 and preferably from 0.4 to 25.

    Abstract translation: 用于降低烟道气中氮氧化物含量的催化剂。 催化剂含有至少一种金属钛,锆,钒,钨,钼或铈,其中一种或多种氧化物与具有三层结构(三层硅酸盐)的硅酸盐形式组合,所述三层结构(三层硅酸盐)选自 由伊利石和云母组成的组。 三层硅酸盐中的硅与氧化物中的金属的原子比为0.2〜50,优选为0.4〜25。

    Method of processing a high-boiling fraction obtained in the cracking of
hydrocarbons
    6.
    发明授权
    Method of processing a high-boiling fraction obtained in the cracking of hydrocarbons 失效
    处理在烃裂解中获得的高沸点馏分的方法

    公开(公告)号:US4244808A

    公开(公告)日:1981-01-13

    申请号:US76828

    申请日:1979-09-19

    CPC classification number: C10G69/06 C10G2400/30

    Abstract: A process for the treatment of a hydrocarbon fraction having a boiling point range beginning above 200.degree. C. and obtained in the cracking of hydrocarbons, in which the polymeric component resulting from the cracking pyrolysis is removed and the remaining polymer-free hydrocarbon is subjected to hydrogenation under such reaction conditions that the product is high in monoaromatic components while the polyaromatics are removed therefrom.

    Abstract translation: 一种处理沸点范围从高于200℃开始并在烃裂解中获得的烃馏分的方法,其中除去由裂解热解产生的聚合物组分,并将剩余的不含聚合物的烃进行 在这样的反应条件下氢化,使产物的单芳族成分高,同时从其中除去多芳族化合物。

    Process for decreasing the content of nitrogen oxides in flue gases
    8.
    发明授权
    Process for decreasing the content of nitrogen oxides in flue gases 失效
    降低烟道气中氮氧化物含量的方法

    公开(公告)号:US4792439A

    公开(公告)日:1988-12-20

    申请号:US47797

    申请日:1987-05-07

    Abstract: A process for decreasing the content of nitrogen oxides in flue gases. The process comprising contacting the flue gases with a catalyst. The catalyst contains at least one of the metals titanium, zirconium, vanadium, tungsten, molybdenum, or cerium in the form of one or more of their oxides combined with a silicate with a layer structure (layer silicate) comprising acid-activated kaolin. The crystalline layer structure of the acid-activated kaolin is essentially retained, while being not yet X-ray amorphous. The acid activation increases the BET surface area at least 15% and preferably at least 50% in terms of the BET surface area of the kaolin before acid activation. The atomic ratio of the silicon in the acid-activated kaolin to the metal in the oxide is from 0.2 and 50 and preferably from 0.4 to 25.

    Abstract translation: 降低烟道气中氮氧化物含量的方法。 该方法包括使烟道气与催化剂接触。 催化剂含有至少一种金属钛,锆,钒,钨,钼或铈,其中一种或多种氧化物与具有含酸活化高岭土的层结构(层状硅酸盐)的硅酸盐结合。 酸活化的高岭土的结晶层结构基本上保持不变,同时还没有X射线无定形。 在酸活化之前,酸活化使得BET表面积以高岭土的BET表面积计增加至少15%,优选至少50%。 酸活化高岭土中的硅与氧化物中的金属的原子比为0.2〜50,优选为0.4〜25。

Patent Agency Ranking