Adsorbent-treated cat cracked gasoline in motor fuels
    132.
    发明授权
    Adsorbent-treated cat cracked gasoline in motor fuels 失效
    吸附剂处理的猫在汽油中的汽油

    公开(公告)号:US4225319A

    公开(公告)日:1980-09-30

    申请号:US922257

    申请日:1978-07-05

    CPC classification number: C10L1/06 C10L1/14 C10L1/1616 C10L1/223 C10L1/232

    Abstract: A method for supressing carburetor deposit formation of motor fuels containing untreated cat cracked gasoline by blending adsorbent-treated cat cracked gasoline into the motor fuel. Up to about 50 percent by weight of the total composition is adsorbent-treated cat cracked gasoline, but preferably from about 5 to about 25 percent by weight of the total composition is adsorbent-treated cat cracked gasoline. In a preferred embodiment a standard reference fuel capable of providing a predetermined level of carburetor deposit formation is provided by the addition of either adsorbent-treated cat cracked gasoline, untreated cat cracked gasoline, or aromatic amines to a base fuel.

    Abstract translation: 一种用于通过将吸附剂处理的猫裂化汽油混合到发动机燃料中来抑制含有未处理的猫裂化汽油的运动燃料的化油器沉积物形成的方法。 吸附处理的猫裂化汽油高达总组合物的约50重量%,但优选总组合物的约5至约25重量%是吸附剂处理的猫裂化汽油。 在优选实施方案中,通过将吸附剂处理的猫裂化汽油,未处理的猫裂化汽油或芳族胺加入到基础燃料中来提供能够提供预定水平的化油器沉积物形成的标准参考燃料。

    Low benzene content gasoline producing process
    133.
    发明授权
    Low benzene content gasoline producing process 失效
    低含苯汽油生产工艺

    公开(公告)号:US4209383A

    公开(公告)日:1980-06-24

    申请号:US961320

    申请日:1978-11-16

    CPC classification number: C10L1/06 C10G2400/02

    Abstract: A process for the production of a gasoline having a low benzene content. A catalytic reformate and a stripped liquid produced in the gas concentration unit of an FCC unit are fractionated in a dehexanizer to concentrate the benzene and C.sub.3 -C.sub.4 olefins these two streams contain into a single stream. This stream is passed into an alkylation zone wherein at least some of the benzene is alkylated with the olefins. The alkylation zone effluent is stripped and recombined with C.sub.7 -plus dehexanizer bottoms stream to form a gasoline product stream.

    Abstract translation: 一种生产苯含量低的汽油的方法。 将催化重整产物和在FCC装置的气体浓度单元中产生的汽提液体在脱脂器中分馏,将这两种物流中的苯和C3-C4烯烃浓缩成单一流。 该物流进入烷基化区,其中至少一些苯用烯烃烷基化。 将烷基化区流出液汽提,并与C7-加脱氢塔塔底物流重组,形成汽油产物流。

    Conversion of low octane number alkylate to high octane gasoline and
aromatics
    134.
    发明授权
    Conversion of low octane number alkylate to high octane gasoline and aromatics 失效
    低辛烷值烷基化物转化为高辛烷值汽油和芳烃

    公开(公告)号:US4179353A

    公开(公告)日:1979-12-18

    申请号:US813365

    申请日:1977-07-06

    CPC classification number: C10L1/06 C10G35/00 C10G61/04 C10G63/02

    Abstract: An intentionally produced low octane value alkylate is reformed in the presence of steam, and in the absence of added hydrogen, to produce a high octane value, olefinic reformate containing aromatics. The reformate, upon fractionation to remove hydrogen and methane and C.sub.3 and C.sub.4 hydrocarbons, which can be recycled, is subjected to solvent extraction to produce a raffinate which can be used as high octane gasoline and which contains olefins, and an extract which, upon fractionation to remove xylenes therefrom as usable product, and which now contains benzene and toluene, can be combined with said raffinate.

    Abstract translation: 有意产生的低辛烷值的烷基化物在蒸汽存在下重整,在没有加入氢气的情况下,产生高辛烷值,含有芳烃的烯烃重整产物。 将可再循环的分解除去氢气和甲烷的重整油和C3和C4烃进行溶剂萃取以产生可用作高辛烷值汽油并含有烯烃的萃余液,以及分馏时的提取物 从其中除去二甲苯作为可用的产物,并且其现在含有苯和甲苯可与所述残液相组合。

    Process to reduce the benzene content of gasoline
    135.
    发明授权
    Process to reduce the benzene content of gasoline 失效
    降低汽油苯含量的方法

    公开(公告)号:US4140622A

    公开(公告)日:1979-02-20

    申请号:US848058

    申请日:1977-11-03

    CPC classification number: C10L1/06 C10G2400/02

    Abstract: Benzene, which is toxic and carcinogenic, is removed from a gasoline or gasoline precursor stream, such as a mixture of a reformate and a naphtha produced in a fluidized catalytic cracking unit, in a process which includes fractionating the precursor stream into a light hydrocarbon stream containing the benzene and a heavy hydrocarbon stream. The light hydrocarbon stream is then admixed with an olefinic hydrocarbon, passed through an alkylation zone and then remixed with the heavy hydrocarbon stream.

    Abstract translation: 具有毒性和致癌性的苯在包括在流化催化裂化装置中产生的重整产物和石脑油的混合物的汽油或汽油前体物流中被除去,包括将前体物流分馏成轻质烃流 含有苯和重质烃流。 然后将轻烃物流与烯烃混合,通过烷基化区,然后与重质烃流混合。

    Method for upgrading products of Fischer-Tropsch synthesis
    138.
    发明授权
    Method for upgrading products of Fischer-Tropsch synthesis 失效
    Fischer-Tropsch合成产品升级方法

    公开(公告)号:US4041094A

    公开(公告)日:1977-08-09

    申请号:US614587

    申请日:1975-09-18

    CPC classification number: C10G59/02 C10G50/00 C10G67/02 C10L1/06 Y10S208/95

    Abstract: Upgrading of Fischer-Tropsch synthesis product is obtained by separating a 560.degree. F minus hydrocarbon fraction from gaseous C.sub.5 rich material and a water phase comprising oxygenates. Alcohols may be recovered from the water phase for conversion to gasoline boiling components. C.sub.5 rich material is converted to gasoline boiling material with a ZSM-5 crystalline zeolite and upgrading of the 560.degree. F minus hydrocarbon fraction is accomplished with a ZSM-5 crystalline zeolite catalyst.

    Abstract translation: 费 - 托合成产物的升级通过从气态C5富含材料和包含含氧化合物的水相中分离560°F减去烃馏分而获得。 醇可以从水相中回收以转化成汽油沸点组分。 使用ZSM-5结晶沸石将富C5的材料转化为汽油沸腾物质,并用ZSM-5结晶沸石催化剂完成560°F减去烃馏分的升级。

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