Process for the desulfurization of petroleum coke
    2.
    发明授权
    Process for the desulfurization of petroleum coke 失效
    石油焦脱硫工艺

    公开(公告)号:US4146434A

    公开(公告)日:1979-03-27

    申请号:US684344

    申请日:1976-05-07

    IPC分类号: C10L9/08 C10B57/00 C01B31/04

    CPC分类号: C10L9/08

    摘要: Delayed coke especially manufactured for use in graphite can be effectively desulfurized by calcining in a hydrocarbon fuel-fired calciner in the temperature range of 2700.degree. F. to 2900.degree. F. without adversely affecting the strength of the coke or the coefficient of thermal expansion of the graphitized coke.

    摘要翻译: 特别是制造用于石墨的延迟焦炭可通过在2700°F至2900°F的温度范围内在烃燃料燃烧煅烧炉中煅烧而有效脱硫,而不会对焦炭的强度或热膨胀系数产生不利影响 石墨化焦炭。

    Recovery of bitumen from tar sands
    5.
    发明授权
    Recovery of bitumen from tar sands 失效
    从沥青砂中回收沥青

    公开(公告)号:US4174263A

    公开(公告)日:1979-11-13

    申请号:US919890

    申请日:1978-06-28

    IPC分类号: C10G1/04

    CPC分类号: C10G1/04

    摘要: Bitumen is separated from tar sands by contacting the tar sands with a small amount of liquid, heating the liquid treated tar sands to expand the liquid as a vapor thereby reducing the density of the bitumen and separating the bitumen from the remainder of the tar sands on the basis of density.

    摘要翻译: 沥青与沥青砂分离,通过将焦油砂与少量液体接触,加热液体处理的焦油砂,以蒸气膨胀液体,从而降低沥青的密度,并将沥青与剩余的焦油砂分离 密度的基础。

    Technique for tertiary oil recovery
    6.
    发明授权
    Technique for tertiary oil recovery 失效
    三次采油技术

    公开(公告)号:US4329236A

    公开(公告)日:1982-05-11

    申请号:US136641

    申请日:1980-04-02

    IPC分类号: C09K8/584 E21B43/22

    CPC分类号: C09K8/584 Y10S507/938

    摘要: The optimal salinity of an emulsifier system comprising an alcohol and a neutralized oxidized solvent extracted oil can be controlled to match the salinity of the brine used in the tertiary oil recovery process by controlling the acid number of the solvent extracted oil during the oxidation procedure, controlling the extent of the neutralization during neutralization of the oxidized solvent extracted oil, or both.

    摘要翻译: 可以通过控制氧化过程中溶剂萃取油的酸值控制包含醇和中和的氧化溶剂萃取油的乳化剂体系的最佳盐度,使其与三次采油过程中所用盐水的盐度相匹配,从而控制 在中和氧化溶剂萃取油中的中和程度,或两者兼而有之。

    Tar sands recovery process
    8.
    发明授权
    Tar sands recovery process 失效
    焦油砂恢复过程

    公开(公告)号:US4067796A

    公开(公告)日:1978-01-10

    申请号:US581317

    申请日:1975-05-27

    IPC分类号: C10G1/04

    CPC分类号: C10G1/047 C10G1/04

    摘要: The present invention is an improved process for the recovery of bitumen from tar sand by employing a vessel containing a liquid comprising an organic phase consisting of a hydrocarbon solvent which is immiscible in water and an aqueous phase. The tar sand optionally containing water is introduced into the organic phase and then subsequently passes into the aqueous phase.

    摘要翻译: 本发明是通过使用含有液体的容器从焦油砂中回收沥青的改进方法,所述液体包含由在水和水相中不混溶的烃溶剂组成的有机相。 任选地含有水的焦油砂被引入有机相中,然后进入水相。

    Treatment of acrylonitrile waste water with activated carbon
    9.
    发明授权
    Treatment of acrylonitrile waste water with activated carbon 失效
    用活性炭处理丙烯腈废水

    公开(公告)号:US4141826A

    公开(公告)日:1979-02-27

    申请号:US782801

    申请日:1977-03-30

    IPC分类号: C02F1/28 C02F9/00 C02C5/02

    CPC分类号: C02F1/283 C02F2101/32

    摘要: Waste water produced in an acrylonitrile plant and containing significant amounts of acrylonitrile and acrylic acid is processed so as to reduce its organics content for disposal purposes and to recover the acrylonitrile and acrylic acid contained therein. The waste water is treated by contact with activated carbon to adsorb the organics contained therein. The activated carbon is periodicaly regenerated with a desorbing liquid and the desorbate product is distilled to yield acrylonitrile and acrylic acid. Every fifth regeneration cycle, the activated carbon is regenerated thermally rather than means of a liquid in order to restore its activity to its original value.

    摘要翻译: 处理在丙烯腈装置中生产的含有大量丙烯腈和丙烯酸的废水,以减少其有机物含量进行处理,并回收其中所含的丙烯腈和丙烯酸。 通过与活性炭接触来处理废水以吸附其中所含的有机物。 活性炭用解吸液定期再生,脱附产物蒸馏得到丙烯腈和丙烯酸。 每五个再生循环中,活性炭是热再生而不是液体的方式,以将其活性恢复到其原始值。

    Process for production of activated carbon
    10.
    发明授权
    Process for production of activated carbon 失效
    活性炭生产工艺

    公开(公告)号:US3994829A

    公开(公告)日:1976-11-30

    申请号:US480434

    申请日:1974-06-17

    申请人: Harvey E. Alford

    发明人: Harvey E. Alford

    IPC分类号: C01B31/08 B01J21/18

    CPC分类号: C01B31/082

    摘要: An improved process for the production in high yield of activated carbon particles of high activity comprises rapid removal of volatile material from the area of carbonaceous particles during the carbonization step by individually venting each hearth of a multiple hearth furnace. The carbonaceous particles which are subjected to the carbonization step are prepared from mixtures of carbonaceous material and petroleum acid sludge.

    摘要翻译: 用于高产率活性炭颗粒高生产率的改进方法包括通过单独排气多个炉床的每个炉床,在碳化步骤期间从碳质颗粒区域快速除去挥发性物质。 进行碳化步骤的碳质颗粒由碳质材料和石油酸性污泥的混合物制备。