Upgrading heavy oils by non-catalytic treatment with hydrogen and
hydrogen transfer solvent
    4.
    发明授权
    Upgrading heavy oils by non-catalytic treatment with hydrogen and hydrogen transfer solvent 失效
    通过氢气和氢转移溶剂的非催化处理来提升重油

    公开(公告)号:US4292168A

    公开(公告)日:1981-09-29

    申请号:US107949

    申请日:1979-12-28

    IPC分类号: C10G47/22 C10G47/34 C10G9/14

    CPC分类号: C10G47/34

    摘要: Heavy liquid hydrocarbon oil, such as petroleum derived tars, predominantly boiling over 425.degree. C., are upgraded to products boiling below 425.degree. C., without substantial formation of insoluble char, by heating the heavy oil with hydrogen and a hydrogen transfer solvent in the absence of hydrogenation catalyst at temperatures of about 320.degree. C. to 500.degree. C., and a pressure of 20 to 180 bar for 3 to 30 minutes. The hydrogen transfer solvents are polycyclic compounds free of carbonyl groups, e.g., pyrene, and have a polarographic reduction potential which is less negative than phenanthrene and equal to or more negative than azapyrene.

    摘要翻译: 重质液体烃油,例如主要沸点超过425℃的石油衍生焦油,通过用氢气和氢转移溶剂加热重质油,升级成沸点低于425℃的产物,不会形成不溶性焦炭 在约320℃至500℃的温度下不存在氢化催化剂,并且压力为20至180巴3至30分钟。 氢转移溶剂是不含羰基的多环化合物,例如芘,并且具有极低于菲的极性还原电位,并且等于或大于氮杂萘的负性。

    Olefin hydrogenation over synthetic amorphous silica
    5.
    发明授权
    Olefin hydrogenation over synthetic amorphous silica 失效
    合成无定形二氧化硅上的烯烃氢化

    公开(公告)号:US4218571A

    公开(公告)日:1980-08-19

    申请号:US041204

    申请日:1979-05-21

    摘要: Hydrogenation-dehydrogenation of suitable feedstock is provided wherein such feedstock is subjected to hydrogenation-dehydrogenation conditions in the presence of a catalytic amount of a solid containing, at least in part, a synthetic amorphous solid prepared by hydrolyzing and polymerizing in the presence of water a silane having the formula R(Si)X.sub.3, wherein R is a nonhydrolyzable organic group, X is a hydrolyzable group and (Si) is selected from the group consisting of ##STR1## and calcining the polymerized product, said silane being admixed with a second component, R'.sub.n MY.sub.m, wherein R' is selected from the group consisting of the same groups as R, Y is selected from the group consisting of the same groups as X and oxygen, M is at least one member selected from the group consisting of the elements of Groups IIIA, IVA, VA, IVB, VB, VIB, VIIB and VIII of the Periodic Table, m is any number greater than 0 and up to 8 and n is from 0 to any number less than 8.

    摘要翻译: 提供合适的原料的氢化 - 脱氢,其中这样的原料在催化量的固体存在下进行氢化 - 脱氢条件,所述固体至少部分地由在水存在下水解和聚合制备的合成非晶态固体 具有式R(Si)X3的硅烷,其中R是不可水解的有机基团,X是可水解基团,(Si)选自和煅烧聚合产物,所述硅烷与第二 组分R'nMYm,其中R'选自与R相同的基团,Y选自与X和氧相同的基团,M是选自由以下组成的组中的至少一个: 元素周期表IIIA,IVA,VA,IVB,VB,VIB,VIIB和VIII族的元素,m是大于0和至多8的任何数,n是0至小于8的任何数。

    Process for coal liquefaction
    7.
    发明授权
    Process for coal liquefaction 失效
    煤液化过程

    公开(公告)号:US4374725A

    公开(公告)日:1983-02-22

    申请号:US903912

    申请日:1978-05-08

    CPC分类号: C10G1/065 C10G1/042

    摘要: In two stage solvent refining of coal by mixing comminuted coal with a solvent produced in the process under hydrogen pressure for initial solubilization and reacting the mixture under hydrogen pressure in a second stage, the overall process is improved by enriching the recycled solvent in hydroaromatic hydrocarbons of fourteen or less carbon atoms.

    摘要翻译: 通过将粉碎煤与在氢气压力下生产的溶剂混合以进行两步溶剂精炼,以初始溶解,并在第二阶段在氢气压力下使混合物反应,整个过程通过富集环烷烃中的再循环溶剂而得到改善 十四个或更少的碳原子。

    Integrated coal liquefication process
    10.
    发明授权
    Integrated coal liquefication process 失效
    综合煤液化过程

    公开(公告)号:US4452688A

    公开(公告)日:1984-06-05

    申请号:US182076

    申请日:1980-08-28

    CPC分类号: C10G1/002 C10G1/006 C10G45/00

    摘要: Hydrogen conservation in solvent refining of coal is practiced and solvent compositions and adjusted to needs of two stage operation. The first stage is a short residence time dissolution in a recycle solvent rich in phenols and polyaromatics of high boiling range. The solvent is enriched for the second stage in low boiling hydrogen donors and the product of the process undergoes hydrotreating in an integrated process.

    摘要翻译: 实施煤溶剂精炼中的氢保存和溶剂组成,并调整为两阶段操作的需要。 第一阶段是在富含酚类和高沸点多芳族化合物的回收溶剂中的短停留时间溶解。 溶剂富集在低沸氢氢供体中的第二阶段,并且该方法的产物在一体化过程中进行加氢处理。