Isomerization process
    1.
    发明授权
    Isomerization process 失效
    异构化过程

    公开(公告)号:US3907913A

    公开(公告)日:1975-09-23

    申请号:US47840674

    申请日:1974-06-11

    Applicant: CHEVRON RES

    Inventor: KEMP JACOB D

    CPC classification number: C07C5/2721

    Abstract: The deactivation rate for a supported acidic catalyst, especially for a supported acid catalyst such as a supported HF.SbF5 catalyst, used in a process for isomerizing a feed comprising methylcyclopentane, cyclohexane, or mixtures thereof, at low temperature, is sharply reduced by including sufficient isobutane in the feed so that the feed isobutane content is 25 to 75 weight percent.

    Abstract translation: 负载型酸性催化剂,特别是用于负载型酸催化剂如负载型HF.SbF5催化剂的失活速率通过包括在低温下异构化包含甲基环戊烷,环己烷或其混合物的进料异构化的方法而急剧减少 进料中足够的异丁烷使得进料异丁烷含量为25至75重量%。

    Jet fuel production
    2.
    发明授权
    Jet fuel production 失效
    喷油燃料生产

    公开(公告)号:US3657377A

    公开(公告)日:1972-04-18

    申请号:US3657377D

    申请日:1970-01-19

    Applicant: CHEVRON RES

    Inventor: KEMP JACOB D

    CPC classification number: C10L1/06

    Abstract: AN ALKYLATION PROCESS FOR PRODUCING JET FUEL FROM HYDROCARBONS WHICH COMPRIES (A) CONTACTING AN ISOPARAFFIN FEEDSTOCK WITH AN OLEFIN FEEDSTOCK IN THE PRESENCE OF HYDROFLUORIC ACID AT A TEMPERATURE BETWEEN ABOUT 30* AND 100* F. IN A REACTION ZONE, (B) MAINTAINING THE RATIO OF ISOPARAFFIN TO OLELIN BELOW 2.0 IN SAID REACTION ZONE, AND (C) WITHDRAWING FROM SAID REACTION ZONE AN EFFLUENT CONTAINING AT LEAST 10 WEIGHT PERCENT HYDROCARBON BOILING BETWEEN ABOUT 300* AND 550*F.,EXCLUSIVE OF ANY ACID OIL PRODUCED IN SAID REACTION ZONE.

    Gasoline production
    4.
    发明授权
    Gasoline production 失效
    汽油生产

    公开(公告)号:US3904384A

    公开(公告)日:1975-09-09

    申请号:US30611772

    申请日:1972-11-13

    Applicant: CHEVRON RES

    CPC classification number: C10L1/023

    Abstract: A process for producing a high-octane gasoline having reduced smog-forming tendencies, which comprises: A. THERMALLY DEHYDROGENATING-CRACKING ISOBUTANE TO OBTAIN PROPYLENE AND ISOBUTENE; B. HYDRATING PROPYLENE TO OBTAIN ISOPROPANOL; C. ETHERATING THE ISOPROPANOL WITH THE ISOBUTENE TO OBTAIN TBUTYL ISOPROPYL ETHER; AND D. BLENDING THE T-BUTYL ISOPROPYL ETHER WITH GASOLINE-BOILINGRANGE HYDROCARBONS. Preferably the thermal dehydrogenation is carried out under conditions, specifically including a temperature between about 1125* and 1275*F., to produce a molar ratio of isobutene to propylene between 1.0 to 1.25.

    Abstract translation: 一种生产具有降低烟雾形成倾向的高辛烷值汽油的方法,其包括:

    Isomerization
    5.
    发明授权
    Isomerization 失效
    异构化

    公开(公告)号:US3903196A

    公开(公告)日:1975-09-02

    申请号:US42262173

    申请日:1973-12-07

    Applicant: CHEVRON RES

    Inventor: KEMP JACOB D

    CPC classification number: C07C5/2789 C07C9/00

    Abstract: The deactivation rate for a supported HF-antimony pentafluoride catalyst, used in a process for isomerizing C5, C6, or C7 normal paraffin at low temperature, is sharply reduced by including sufficient isobutane in the feed so that the feed isobutane content is more than 25 weight per cent.

    Abstract translation: 在低温下用于异构化C5,C6或C7正链烷烃的方法中用于负载的五氟化锑 - 五氟化锑催化剂的失活速率通过在进料中包含足够的异丁烷使得进料异丁烷含量大于25而急剧降低 重量百分比。

    Process for the esterification of isobutene
    6.
    发明授权
    Process for the esterification of isobutene 失效
    ISOBUTENE的确定过程

    公开(公告)号:US3678099A

    公开(公告)日:1972-07-18

    申请号:US3678099D

    申请日:1970-06-26

    Applicant: CHEVRON RES

    Inventor: KEMP JACOB D

    CPC classification number: C07C51/14 C07C67/04 C07C67/56 C07C69/06 C07C69/14

    Abstract: A process for the esterification of isobutene with reduced polymerization of the isobutene which comprises contacting the isobutene with a lower carboxylic acid and an acidic resin catalyst containing a sulfonate group, which catalyst has between about 0.2 and 2.4 meq. of H+ per gram of catalyst. Preferred carboxylic acids include formic acid and acetic acid and the preferred type catalyst is a resinous sulfonated polystyrene divinyl benzene copolymer.

    Abstract translation: 一种异丁烯酯化反应的方法,其中异丁烯的聚合反应降低,其中包括使异丁烯与低级羧酸和含有磺酸酯基的酸性树脂催化剂接触,该催化剂具有约0.2至2.4meq。 的H +每克催化剂。 优选的羧酸包括甲酸和乙酸,优选的类型催化剂是树脂磺化聚苯乙烯二乙烯基苯共聚物。

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