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    Removal of organic compounds from coker gasoline
    52.
    发明授权
    Removal of organic compounds from coker gasoline 失效
    从焦化汽油中除去有机化合物

    公开(公告)号：US4176047A

    公开(公告)日：1979-11-27

    申请号：US894978

    申请日：1978-04-10

    Applicant: Derrell D. Orrell ,  Melvin M. McFeeters

    Inventor： Derrell D. Orrell ,  Melvin M. McFeeters

    IPC: C10G25/00 ,  C10G29/16 ,  C10G61/06 ,  C10G63/04 ,  C10G37/00

    CPC classification number: C10G25/00 ,  C10G2400/02

    Abstract: A gasoline boiling range hydrocarbon stream obtained by fractionation of overhead vapors from a delayed coker is treated for removal of organic silicon compounds prior to being processed in a desulfurizer and catalytic reformer. The stream is treated by a bed of material such as alumina, activated alumina or spent alumina-based desulfurizer catalyst at elevated temperature to reduce the level of organic silicon compounds. The organic silicon compounds, if not removed, are detrimental to desulfurizer and reformer catalysts. The organic silicon compounds are conventionally added to a delayed coker to control foaming.

    Abstract translation: 在脱硫剂和催化重整器中处理之前，处理通过从延迟焦化器中分馏塔顶蒸气获得的汽油沸程烃流去除有机硅化合物。 该物流通过诸如氧化铝，活性氧化铝或废氧化铝基脱硫剂催化剂的材料床在升高的温度下处理以降低有机硅化合物的含量。 有机硅化合物（如果不除去）对脱硫剂和重整器催化剂是不利的。 通常将有机硅化合物加入到延迟焦化器中以控制发泡。

    Process for the reclamation of waste hydrocarbon oils
    53.
    发明授权
    Process for the reclamation of waste hydrocarbon oils 失效
    废烃油回收方法

    公开(公告)号：US4124492A

    公开(公告)日：1978-11-07

    申请号：US829637

    申请日：1977-09-01

    Applicant: David T. Fung ,  J. G. Jacques Laberge ,  Frederick S. Przystal

    Inventor： David T. Fung ,  J. G. Jacques Laberge ,  Frederick S. Przystal

    IPC: C10G21/16 ,  C10G7/04 ,  C10G53/04 ,  C10G53/08 ,  C10M175/00 ,  C10G37/00 ,  C10M11/00

    CPC classification number: C10M175/005 ,  C10G7/04 ,  C10G2400/10

    Abstract: Disclosed is a process for rejuvenating and reclaiming useful hydrocarbon oils from contaminated waste oils. The process comprises dehydrating the waste oil and thereafter dissolving the dehydrated oil in a selected amount of isopropanol or N-propanol at a temperature of from 45.degree. C. to 80.degree. C. The undissolved waste matter is separated and the residual oil/solvent fraction is distilled to recover the decontaminated oil and the solvent. The recovered oil can be further clarified by treatment with a bleaching clay or activated carbon at elevated temperatures. The process is more efficient and economic than those known heretofore resulting in high yields of reclaimed oil and more environmentally acceptable waste products.

    Abstract translation: 公开了一种从受污染的废油中再生和回收有用的烃油的方法。 该方法包括使废油脱水，然后在45℃至80℃的温度下将脱水油溶解在选定量的异丙醇或N-丙醇中。分离出未溶解的废物，残留的油/溶剂馏分 蒸馏除去去污的油和溶剂。 回收的油可以通过在高温下用漂白粘土或活性炭处理进一步澄清。 该方法比迄今为止已知的再生油和更环境可接受的废产物的高产量更有效和经济。

    Production of low sulfur fuel oil and hydrogen from petroleum residium
    54.
    发明授权
    Production of low sulfur fuel oil and hydrogen from petroleum residium 失效
    从石油生产低硫燃料油和氢气

    公开(公告)号：US3972803A

    公开(公告)日：1976-08-03

    申请号：US443025

    申请日：1974-02-15

    Applicant: Ronald H. Wolk ,  Axel R. Johnson ,  Govanon Nongbri

    Inventor： Ronald H. Wolk ,  Axel R. Johnson ,  Govanon Nongbri

    IPC: C01B3/22 ,  C01B3/36 ,  C01B3/38 ,  C10G45/16 ,  C10G65/12 ,  C10G69/00 ,  C10G37/00 ,  C10G23/10

    CPC classification number: C01B3/382 ,  C01B3/22 ,  C01B3/36 ,  C01B3/38 ,  C10G2300/107

    Abstract: In producing low sulfur fuel oil by the ebullated bed hydroconversion of petroleum residue, the resulting heavy vacuum bottoms sulfur-containing residue material is utilized to produce hydrogen. The residue material from the hydroconversion operation is gasified to provide a fuel gas, which is then used to fire a steam-methane reformer. The chemical requirements for hydrogen production are met by feeding a portion of light gaseous products from the hydroconversion step to the catalytic side of the steam-methane reformer. A low sulfur fuel oil distillate product is recovered from the reactor effluent streams and can be further hydrotreated as desired. Thus, all hydrogen required in the H-Oil reactor for hydroconversion and desulfurization is ultimately produced from the residual oil feed material, by using the heavy product residue material to produce a fuel gas and converting the light hydrocarbons to hydrogen.

    Abstract translation: 通过石油残渣的沸腾床加氢转化来生产低硫燃料油时，所得到的重真空塔底含硫残渣物质用于生产氢气。 来自加氢转化操作的残余物质被气化以提供燃料气体，然后将其用于燃烧蒸汽 - 甲烷重整器。 通过将来自加氢转化步骤的轻质气态产物的一部分进料到蒸汽 - 甲烷重整器的催化侧来满足制氢的化学需求。 从反应器流出物流中回收低硫燃料​​油馏出物产物，并且可以根据需要进一步加氢处理。 因此，用于加氢转化和脱硫的H-油反应器中所需的所有氢气最终由剩余的油进料通过使用重的产物残余物质产生燃料气体并将轻质烃转化为氢来产生。

    Production of lubricating oils
    55.
    发明授权
    Production of lubricating oils 失效
    生产润滑油

    公开(公告)号：US3968023A

    公开(公告)日：1976-07-06

    申请号：US545655

    申请日：1975-01-30

    Applicant: Tsoung-Yuan Yan

    Inventor： Tsoung-Yuan Yan

    IPC: C10G67/14 ,  C10G37/00

    CPC classification number: C10G67/14 ,  C10G2400/10

    Abstract: Residual oils are upgraded to lube oil base stocks by a combination process involving deasphalting, solvent extraction and hydrocracking arranged to particularly promote the efficient production of lube oil products.

    Abstract translation: 剩余油通过脱沥青，溶剂萃取和加氢裂化的组合方法升级为润滑油基础油，以便特别促进润滑油产品的有效生产。

    Producing coke from hydrotreated crude oil
    57.
    发明授权
    Producing coke from hydrotreated crude oil 失效
    从加氢原油生产焦糖

    公开(公告)号：US3775294A

    公开(公告)日：1973-11-27

    申请号：US3775294D

    申请日：1971-06-28

    Applicant: MARATHON OIL CO

    Inventor： PETERSON A ,  DORMISH F

    IPC: C10B55/00 ,  C10G37/00

    CPC classification number: C10B57/04 ,  C10B55/00

    Abstract: D R A W I N G
    WHOLE SOUR CRUDE OIL TOGETHER WITH C5-PLUS LIQUID PRODUCTS FROM A COKER ARE HUDROTREATED PRIOR TO SEPARATION INTO VARIOUS BOILING-RANGE PRODUCTS. THE RESIDUAL MATERIAL FROM THIS DISTILLATION IS COKED TO OBTAIN LOW SULFUR COKE AND LIQUID PRODUCTS OF WHICH THE C5-PLUS PORTION IS RECYCLED TO COMMINGLE WITH THE CRUDE OIL PRIOR TO HYDROTREATING. OPTIONALLY, THE CRUDE OIL MAY BE TOPPED TO REMOVE FRACTIONS BOILING IN THE RANGE OF FROM THE INITIAL BOILING POINT OF THE CRUDE TO ABOUT 400*F., PRIOR TO HYDROTREATING.

    Hydrocracking production of lubes
    58.
    发明授权
    Hydrocracking production of lubes 失效
    水压生产

    公开(公告)号：US3723295A

    公开(公告)日：1973-03-27

    申请号：US3723295D

    申请日：1970-08-17

    Applicant: SUN OIL CO

    Inventor： KRESS R

    IPC: C10G21/00 ,  C10G67/00 ,  C10G67/04 ,  C10G37/00

    CPC classification number: C10G21/00 ,  C10G2400/10

    Abstract: A PROCESS FOR PREVARING HIGH V.I. LUBE OILS OF IMPROVED QUALITY COMPRISING SOLVENT EXTRACTING AT LEAST PART OF THE LUBE OIL HYDROCRACKER CHARGE STOCK WITH A SOLVENT HAVING PREFERENTIAL SOLUBILITY FOR AROMATICS, FOR EXAMPLE, FURFURAL; HYDROCRACKING THE RAFFINATE FROM SAID EXTRACTION UNDER CONDITIONS PROVIDING FOR AN INCREASED V.I. OF SAID RAFFINATE. QUALITY IS FURTHER ENHANCED BY SERIALLY EXTRACTING THE HYDROCRACKED PRODUCTS WITH A SOLVENT HAVING PREFERENTIAL SOLUBILITY FOR AROMATICS, SUCH AS FURFURAL, UNDER CONDITIONS PROVIDING FOR HIGHLY SELECTIVE REMOVAL OF COLOR BODIES, COLOR BODY PRECURSORS, U.V. ADSORBING COMPOUNDS AND SLUDGE PRECURSORS. ALTERNATIVELY, THE QUALITY OF THE HYDROCRACKED PRODUCT MAY BE FURTHER ENHANCED BY SELECTIVELY HYDROGENATING SAME AT RELATIVELY SEVERE LUBE HYDROGENATION CONDITIONS WHEREBY COLOR BODIES, COLOR BODY PRECURSORS, U.V. ADSORBING COMPOUNDS AND SLUDGE PRECURSORS ARE MITIGATED.
    D R A W I N G

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