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公开(公告)号：US3847792A
公开(公告)日：1974-11-12
申请号：US40534873
申请日：1973-10-10
Applicant: UNIVERSAL OIL PROD CO
Inventor： BERGER C
CPC classification number: C10G59/02
Abstract: A combination process for the production of an unleaded, narrow boiling range, high octane motor fuel which involves (1) a novel form of low-severity hydrocracking followed by (2) catalytic reforming. The process is effected without the intermediate separation of the product effluent from the low-severity hydrocracking zone, and, therefore, provides a true ''''in-line'''' hydrocracking/reforming combination process.
Abstract translation: 用于生产无铅，窄沸点，高辛烷值运动燃料的组合方法，其包括（1）低严重性加氢裂化的新形式，随后是（2）催化重整。 该方法在不将产物流出物从低严重性加氢裂化区中间分离的情况下进行，因此提供真正的“在线”加氢裂化/重整组合方法。
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公开(公告)号：US3803028A
公开(公告)日：1974-04-09
申请号：US35427673
申请日：1973-04-25
Applicant: TEXACO INC
CPC classification number: C10G49/007 , C10G2400/10
Abstract: The viscosity index of a lubricating oil is improved by contacting the oil at elevated temperature and pressure with a catalyst having hydrogenation activity in the presence of hydrogen and in the presence of carbon monoxide.
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公开(公告)号：US3794580A
公开(公告)日：1974-02-26
申请号：US3794580D
申请日：1973-02-26
Applicant: SHELL OIL CO
Inventor： LADEUR P
IPC: C10M109/02 , B01J37/02 , B01J37/20 , B01J37/26 , C10G47/00 , C10G47/20 , C10N20/02 , C10N60/02 , C10G13/02 , C10G37/10
CPC classification number: B01J37/26 , B01J37/0201 , B01J37/20 , C10G2400/10
Abstract: A CATALYTIC HYDROCRACKING PROCESS FOR PRODUCING HIGH VISCOSITY INDEX LUBRICATING OILS BY CONTACTING A MIXTURE OF HEAVY HYDROCARBONS HAVING A NITROGEN CONTENT LESS THAN 3000 P.P.M.W. WITH A CATALYST IN THE PRESENCE OF HYDROGEN UNDER HYDROCRACKING CONDITIONS AND ADDING TO SAID MIXTURE OF HYDROCARBONS UP TO ABOUT 300 P.P.M.W OF AMMONIA OR A NITROGEN COMPOUND WHICH YIELDS AMMONIA UNDER THE CONDITIONS OF THE PROCESS.
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公开(公告)号：US3719586A
公开(公告)日：1973-03-06
申请号：US3719586D
申请日：1971-05-24
Applicant: SUN OIL CO
Inventor： BENNER R
Abstract: LIGHT AND HEAVY NAPHTHA FRACTIONS ARE CONVERTED BY HYDROREFORMING AND HYDROCRACKING TO HIGH QUANTITY MOTOR FUEL IN HIGH YIELD. LIGHT NAPHTHA (180-400* F.) IS REFORMED CATALYTICALLY AND THE STABILIZED REFORMATE BLENDED WITH HEAVY NAPHTHA (400 TO 500* F.). THE MIXTURE IS
HYDROCRACKED IN THE PRESENCE OF PD-ZEOLITE CATALYST AT 650-800* F. HYDROCRACKATE (180-400* F.) IS FURTHER REFORMED CATALYTICALLY.-
公开(公告)号：US3679574A
公开(公告)日：1972-07-25
申请号：US3679574D
申请日：1971-02-25
Applicant: ROBERT L IRVINE
Inventor： IRVINE ROBERT L
CPC classification number: C10G45/16 , C10G2300/107
Abstract: THE INVENTION RELATES TO THE PREPARATION OF LUBE OIL AND WAX FROM LOW VANADIUM CONTENT CRUDE OR RESIDUA FEED. THE FEED IS FIRST TREATED IN A CATALYST DISCARD ZONE HYDROCRACKER USING CATALYST PROVIDED BY REGNERATION OF LOW ACTIVITY CATALYST FROM A SUBSEQUENT MAIN HYDROCRACKING ZONE. THE DISCARD HYDROCRACKER COMPRISING A PLURALITY OF BEDS CONTAINING FLUIDISED CATALYST DESCENDING IN COUNTERCURRENT TO ASCENDING FEED AND HYDROGEN. CATALYST TRANSFER BETWEEN BEDS IS EXTERNAL OF THE REACTOR.
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Patent Agency Ranking
公开(公告)号：US3625879A
公开(公告)日：1971-12-07
申请号：US3625879D
申请日：1970-01-07
Applicant: GULF RESEARCH DEVELOPMENT CO
Inventor： HORNE WILLIAM A , LUZAR RONALD V
Abstract: A process for the production and recovery of benzene from pyrolysis naphtha produced by high-temperature cracking of ethane, propane, naphtha or gas oil to produce ethylene. The process comprises the steps of hydrogenating a selected cut of pyrolysis naphtha to saturate olefins, reforming the hydrocarbon product from the hydrogenation step to convert benzene precursors to aromatic compounds and partially crack the nonaromatic hydrocarbons present and thereafter hydrodealkylating the hydrocarbon product from the reforming step to convert the alkyl aromatics to benzene and further crack nonaromatic compounds including those boiling at about the benzene boiling point, so that benzene may then be separated from the hydrodealkylation effluent by conventional distillation.
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公开(公告)号：US3494855A
公开(公告)日：1970-02-10
申请号：US3494855D
申请日：1968-06-10
Applicant: UNIVERSAL OIL PROD CO
Inventor： STINE LAURENCE O , STOLFA FRANK
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公开(公告)号：US5294328A
公开(公告)日：1994-03-15
申请号：US922935
申请日：1992-07-31
Applicant: Robert J. Schmidt , Paula L. Bogdan , J. W. Adriaan Sachtler , Srikantiah Raghuram
Inventor： Robert J. Schmidt , Paula L. Bogdan , J. W. Adriaan Sachtler , Srikantiah Raghuram
Abstract: A process combination is disclosed to reduce the aromatics content of a key component of gasoline blends. Paraffins contained in catalytic reformates are conserved and upgraded by separation and isomerization, reducing the reforming severity required to achieve a given product octane with concomitant reduction in paraffin aromatization and cracking. Light reformate may be separated and isomerized, and heavier paraffins are separated from the reformate by solvent extraction or adsorption; the recovered heavy paraffins are isomerized, optionally at a substoichiometric hydrogen ratio. A gasoline component having a reduced aromatics content relative to reformate of the same octane number is blended from the net products of the separation and isomerization steps.
Abstract translation: 公开了一种方法组合以降低汽油混合物的关键组分的芳族化合物含量。 包含在催化重整产物中的石蜡通过分离和异构化被保存和升级，降低了获得给定产物辛烷值同时降低链烷烃芳构化和开裂所需的重整严重性。 轻质重整油可以分离和异构化，并且较重的链烷烃通过溶剂萃取或吸附与重整油分离; 回收的重链烷烃异构化，任选地以亚化学计量比的氢气比。 从分离和异构化步骤的净产物中混合相对于相同辛烷值的重整产物具有降低的芳族化合物含量的汽油组分。
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公开(公告)号：US4190519A
公开(公告)日：1980-02-26
申请号：US954064
申请日：1978-10-23
Applicant: Stephen J. Miller , Thomas R. Hughes
Inventor： Stephen J. Miller , Thomas R. Hughes
Abstract: A straight-run naphtha is fractionated at about 66.degree. C., which is just below the boiling point of methylcyclopentane. The 66.degree. C.+ fraction is reformed, and at least a portion of the reformate combined with the 66.degree. C.- fraction and reacted under aromatization conditions over a ZSM-5-type catalyst to form a C.sub.5 + product rich in aromatics. The C.sub.5 + aromaticized product and the remaining reformate can be either sent for BTX recovery or used as a high-octane component of a gasoline blending pool.
Abstract translation: 直馏石脑油在约66℃下分馏，其温度低于甲基环戊烷的沸点。 将66℃+馏分重整，至少部分重整产物与66℃馏分相结合，并在芳构化条件下在ZSM-5型催化剂上反应形成富含芳族化合物的C5 +产物。 可以将C5 +芳族化合物和剩余的重整产物用于BTX回收或用作汽油混合池的高辛烷值组分。
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公开(公告)号：US4176049A
公开(公告)日：1979-11-27
申请号：US892938
申请日：1978-04-03
Applicant: William E. Winter , William L. Schuette
Inventor： William E. Winter , William L. Schuette
CPC classification number: C10G11/05 , C10G2400/02
Abstract: A process which comprises recracking a cracked naphtha feed containing up to about 60 percent, suitably from about 20 to about 40 percent olefins, over a crystalline aluminosilicate zeolite catalyst to further crack the naphtha and saturate at least about 50 percent of the olefins, preferably from about 90 percent to about 100 percent of the olefins, based on the weight of said cracked naphtha feed. In a preferred combination a gas oil is catalytically cracked in a first stage to produce a cat cracked naphtha product of high olefin content, and an intermediate boiling component thereof is recracked as a feed in a second stage over a zeolite catalyst to saturate the olefins, and hydrodenitrogenate and hydrodesulfurize said cat cracked naphtha. The recracked cat cracked naphtha is then hydrotreated at low to mild severities and then catalytically reformed (hydroformed) to produce high octane gasoline.
Abstract translation: 一种方法，其包括将超过约60％（优选约20至约40％的烯烃）的裂化石脑油原料重结晶在结晶硅铝酸盐沸石催化剂上，以进一步裂化石脑油并使至少约50％的烯烃饱和 约90％至约100％的烯烃，基于所述裂化石脑油进料的重量。 在优选的组合中，瓦斯油在第一阶段被催化裂化以产生高烯烃含量的催化裂化石脑油产物，其中间沸点组分作为进料在第二阶段中重新沸石沸石催化剂以使烯烃饱和， 加氢脱氮和加氢脱硫所述猫裂解石脑油。 然后将重新开裂的猫裂解的石脑油加热处理至低至轻微的严重程度，然后催化重整（液压成型）以产生高辛烷值汽油。
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