Process for preparing a monoalkyl aromatic

    公开(公告)号:US3778415A

    公开(公告)日:1973-12-11

    申请号:US3778415D

    申请日:1971-08-13

    Inventor: KO D

    CPC classification number: C07C15/085 B01J19/0006 Y10S585/901 Y10S585/954

    Abstract: AN IMPROVEMENT IN A PROCESS WHEREIN A FIRST COMPOUND AND A SECOND COMPOUND REACT WITH EACH OTHER TO PRODUCE A THIRD COMPOUND AND A FOURTH COMPOUND IN ESSENTIALLY IRREVERSIBLE REACTIONS AND THE SECOND AND FOURTH COMPOUNDS REACT WITH EACH OTHER TO PRODUCE THE THIRD COMPOUND IN EQUILIBRIUM-LIMITED REACTIONS, THE SECOND COMPOUND BEING PRESENT IN THE REACTION MIXTURE IN EXCESS OF THAT REQUIRED FOR THE REACTIONS, AND THE EXCESS AMOUNT OF THE SECOND COMPOUND IS RECYCLED TO THE REACTION ZONE, WHICH INVOLVES REDUCING THE AMOUNT OF THE SECOND COMPOUND IN THE REACTION MIXTURE, INTRODUCING THEREIN THE FOURTH COMPOUND IN AN AMOUNT GREATER THAN WOULD BE PRESENT AT EQUILIBRIUM AND TERMINATING THE PROCESS BEFORE THE REACTION MIXTURE REACHES EQUILIBRIUM.

    Reaction of ketoximes with carboxylic acid amide-sulfur trioxide complexes
    32.
    发明授权
    Reaction of ketoximes with carboxylic acid amide-sulfur trioxide complexes 失效
    羧酸与三羧酸酰硫化物复合物的反应

    公开(公告)号:US3776901A

    公开(公告)日:1973-12-04

    申请号:US3776901D

    申请日:1968-04-01

    Inventor: KELLY K MATTHEWS J

    CPC classification number: C07D201/04

    Abstract: A METHOD FOR CONVERTING A KETOXIME TO AN N-SUBSTITUTED AMIDE BY REACTING A KETOXIME WITH A COMPLEX OF AN NSUBSTITUTED CARBOXYLIC ACID AMIDE AND SULFUR TRIOXIDE TO FORM A NOVEL COMPOUND OF THE KETOXIME, CARBOXYLIC ACID AMIDE AND SULFUR TRIOXIDE AND DECOMPOSING THIS COMPOUND TO PRODUCE AN N-SUBSTITUTED AMIDE CORRESPONDING TO THE KETOXIME. CYCLOHEXANONE OXIME IS CONVERTED TO CAPROLACTAM.

    Reactivity control in petrochemical and refinery processes
    33.
    发明授权
    Reactivity control in petrochemical and refinery processes 失效
    石油化工和炼油工艺中的反应性控制

    公开(公告)号:US3775494A

    公开(公告)日:1973-11-27

    申请号:US3775494D

    申请日:1971-11-26

    Inventor: CARR N

    CPC classification number: B01J19/0006 C07C5/10 C07C2601/14 C07C13/18

    Abstract: A METHOD FOR CONTROLLING A HYDROGENATION PLANT TO AVOID LOCALIZED REACTOR HOT SPOTS AND TO AVOID REACTOR RUN-AWAY AND CATALYST DETERIORATION CAUSED THEREBY IS DISCLOSED FOR SUCH PLAANT INCLUDING A REACTOR AND CATALYST SYSTEM FOR PRODUCING A SATURATED HYDROCARBON FROM A CORRESPONDING UNSATURATED HYDROCARBON. THE METHOD COMPRISES THE STEPS OF SUPPLYING GASEOUS HYDROGEN AND LIQUID UNSATURATED HYDROCARBON FOR THE REACTOR AND CATALYST SYSTEM, SUPPLYING A RECYCLE PORTION OF A PRODUCT OF SAID SYSTEM INCLUDING SUCH SATURATED HYDROCARBON FOR THE INLET OF SAID REACTOR AND CATALYST SYSTEM, SUPPLYING AT LEAST THE LIQUID UNSATURATED HYDROCARBON AND ANY LIQUID PORTION OF SAID RECYCLE PORTION TO THE SYSTEM IN HEAT EXCHANGE RELATION WITH AN EFFLUENT STREAM OF THE SYSTEM, HEAT EXCHANGING THE UNSATURATED HYDROCARBON AND THE RECYCLE PORTION PRIOR TO INLETTING THE REACTOR SYSTEM AND CONTROLLING THE FLOW RATE THEREOF INTO SAID REACTOR SYSTEM SO THAT THE TEMPERATURE OF ALL MATERIALS ENTERING THE SYSTEM INCLUDING THE RECYCLE PORTION IS ABOVE THE DEW POINT OF THE MIXTURE COMPRISING THE TOTAL REACTOR

    FLUID, AND CONTROLLING THE TEMPERATURE OF THESE MATERIALS INCLUDING THE RECYCLE PORTION THROUGHOUT EVERY PORTION OF THE REACTOR AND CATALYST SYSTEM SO THAT THE TEMPERATURES REMAIN CONTINUALLY ABOVE THE DEW POINTS OF ALL OF THE MATERIALS AND THAT ALL MATERIALS ENTERING THE SYSTEM ARE MAINTAINED ENTIRELY IN THEIR GASEOUS PHASE UNIFORMLY THROUGHOUT THE SYSTEM.

    Hydrodesulfurization process for producing a heavy asphaltic fuel oil
    34.
    发明授权
    Hydrodesulfurization process for producing a heavy asphaltic fuel oil 失效
    用于生产重型沥青燃料油的加氢脱硫方法

    公开(公告)号:US3775305A

    公开(公告)日:1973-11-27

    申请号:US3775305D

    申请日:1971-12-08

    CPC classification number: C10G65/04 C10G2300/107

    Abstract: ASPHALT-CONTAINING OILS ARE HYDRODESULFURIZED TO BELOW A REFRACTORY SULFUR LEVEL WITHOUT EXCESSIVELY CONVERTING THE ASPHALT PRESENT BY EMPLOYING A TWO-STAGE HYDRODESULFURIZATION SYSTEM WITH INTERSTAGE HYDROGEN SULFIDE AND LIGHT OIL REMOVAL, WHEREIN THE AVERAGE HYDROGEN PARTIAL PRESSURE IN EACH HYDROESULFURIZATION STAGE IS MAINTAINED SUFFICIENTLY HIGH THAT THE AVERAGE REACTION RATE CONSTANT IS IMPROVED BY A TWO-STAGE OPERATION, BUT SUFFICIENTLY LOW SO THAT NOT LESS THAN ABOUT 50 PERCENT BY WEIGHT OF THE FEED IS RECOVERED AS A PRODUCT BOILING ABOVE THE I.B.P. OF THE FEED.

    Article coated with fluorinated polymer
    35.
    发明授权
    Article coated with fluorinated polymer 失效
    涂有氟化聚合物的物品

    公开(公告)号:US3770493A

    公开(公告)日:1973-11-06

    申请号:US3770493D

    申请日:1972-02-28

    Inventor: GILBERT R

    CPC classification number: C08F8/20 Y10T428/3154 Y10T428/31692 C08F10/00

    Abstract: Coated articles are prepared in which a fibrous web, wood, or metal substrate is coated with a fluorohydrocarbon polymer prepared by fluorinating a hydrocarbon polymer containing trans unsaturation, prepared by deacetylation of an ethylene-vinyl acetate copolymer, with a lead oxide - hydrogen fluoride fluorinating agent.

    Abstract translation: 制备涂布制品,其中纤维网,木材或金属基材用氟化烃聚合物涂覆,氟化烃聚合物通过氟化含氧反应 - 氟化氢氟化氟乙烯 - 乙酸乙烯酯共聚物脱乙酰制备的含有反式不饱和的烃聚合物 代理商

    Method of preparing stable copolymers of ethylene and at least one ethylenically unsaturated carboxylic acid and the product obtained thereby
    38.
    发明授权
    Method of preparing stable copolymers of ethylene and at least one ethylenically unsaturated carboxylic acid and the product obtained thereby 失效
    制备乙烯和至少一种乙烯基不饱和羧酸的稳定共聚物的方法及其获得的产物

    公开(公告)号:US3769261A

    公开(公告)日:1973-10-30

    申请号:US3769261D

    申请日:1972-05-08

    CPC classification number: C08F8/00 C08F20/12

    Abstract: A METHOD OF MAKING A COPOLYMER OF ETHYLENE AND AT LEAST ONE ETHYLENICALLY UNSATURATED CARBOXYLIC ACID COMPRISING THE STEPS OF FIRST THERMALLY DECOMPOSING THE ESTER MOIETIES OF A COPOLYMER OF ETHYLENE AND THE ISOPROPYL ESTER OF AT LEAST ONE ETHYLENICALLY UNSATURATED CARBOXYLIC ACID AND THEREAFTER CONTACTING THE THERMALLY DECOMPOSED COPOLYMER WITH A DIAMINE. THE RESULTING ETHYLENE-CARBOXYLIC ACID COPOLYMER EXHIBITS A STORAGE STABLE MELT INDEX. THE DIAMINE CONTACTING MAY BE ACCOMPLISHED WITH EITHER AN AQUEOUS SOLUTION OF A SUITABLE DIAMINE OR A VAPOR THEREOF. WHEN AN AQUEOUS SOLUTION IS EMPLOYED, THE CONTACTING WILL GENERALLY BE ACCOMPLISHED AT A TEMPERATURE BETWEEN ABOUT 0 AND 50*C. WHILE A TEMPERATURE BETWEEN 20 AND 100*C. WILL BE USED FOR VAPOR PHASE CONTACTING. THE CONTACTING TIME IS, GENERALLY, SHORT AND THE COPOLYMER PRODUCT WILL CONTAIN LESS THAN 5000 P.P.M. BY WEIGHT DIAMINE, PREFERABLY LESS THAN 1000 P.P.M. AND MOST PREFERABLY LESS THAN 100 P.P.M.

    Reforming process
    40.
    发明授权
    Reforming process 失效
    改造工艺

    公开(公告)号:US3748256A

    公开(公告)日:1973-07-24

    申请号:US3748256D

    申请日:1971-08-23

    Inventor: KO D STAHLFELD D

    CPC classification number: C10G59/02

    Abstract: A C5+ NAPHTHA CONTAINING C6 THROUGH C10 AND EVEN C11 AND C12 NAPHTHENES AND LINEAR (NON-RING STRUCTURE) PARAFFINS IS REFORMED TO IMPROVE ITS OCTANE VALUE BY PASSAGE THROUGH ONE OR A PLURALITY OF RELATIVELY HIGH PRESSURE ACIDIC PLATINUM CATALYST NAPHTHENE AROMATIZATION REACTORS IN SERIES WITH ONE OR MORE RELATIVELY LOWER PRESSURE PARAFFIN DEHYDROCYCLIZATION CATALYST REACTORS. MOST C9 AND C10 LINEAR PARAFFINS HAVE AN EXTREMELY LOW OCTANE VALUE (THE OCTANE NUMBER OF NORMAL DECANE IS - 53) AND MUST GENERALLY BE CRACKED TO HIGHER OCTANE NUMBER FRAGMENTS OR TO GASES TO ACHIEVE A GASOLINE PRODUCT OF SATISFACTORY OCTANE NUMBER. IN THE PRIOR ART THIS CRACKING GENERALLY OCCURRED IN THE ACIDIC PLATINUM CATALYST PHASE WHEREIN THE HYDROGEN PRESSURE IS HIGH, PROTECTING THE CATALYST FROM EXCESSIVE COKING. CRACKING OF THE C9 AND C10 PARAFFINS IN THE DEHYDROCYCLIZATION PHASE WHEREIN THE TOTAL PRESSURE IS LOWER IN ORDER TO FAVOR DEHYDROCYCLIZATION IN ADDITION TO DEHYDROGENATION WOULD RESULT IN SEVERE COKING OF CATALYST. ACCORDING TO THIS INVENTION C9 AND C10 LINEAR PARAFFINS ARE NOT HYDROCRACKED BUT RATHER ARE DEHYDROCYCLIZED. IT HAS NOW BEEN DISCOVERED THAT THE DEHYDROCYCLIZATION PHASE MUST DEHYDROCYCLIZE C9 AND C10 PARAFINS TO C9 AND C10 AROMATICS IF THERE IS TO BE AN INCREASE IN OCTANE-BARREL VALUE IN THE DEHYDROCYCLIZATION PHASE. ACCORDING TO THE PRESENT PROCESS, THE C9 AND C10 PARAFFINS ARE NOT CRACKED IN THE HIGH PRESSURE PASE BUT ARE CHARGED TO THE LOW PRESSURE DEHYDROCYCLIZATION CATALYST PHASE WHEREIN THE PRESSURE IS SUFFICIENTL Y LOW TO DEHYDROCYCLIZATION THE C9 AND C10 PARAFFINS SO THAT THERE IS A NET INCREASE IN C9 AND C10 AROMATICS IN THE DEHYDROCYCLIZATION PHASE. THE PRESSURE IN THE DEHYDROCYCLIZATION PHASE IS SUFFICIENTLY LOW THAT THERE IS RELATIVELY LITTLE OR NO NET INCREASE IN C6 AND C7 AROMATICS AT LEAST IN THE ZONE OF THE DEHYDROCYCLIZATION PHASE WHEREIN DEHYDROAROMATIZATION OF C9 AND C10 PARAFFINS OCCURS. IT HAS NOW BEEN DISCOVERED THAT A SIGNIFICANT NET INCREASE OF C9 AND C10 AROMATICS IS INCOMPATIBLE WITH A SIGNIFICANT NET INCREASE IN C6 AND C7 AROMATICS IN THE SAME DEHYDROCYCLIZATION ZONE, AND VICE VERSA. IT HAS FURTHER BEEN DISDISCOVERED THAT DEHYDROCYCLIZATION OF C9 AND C10 LINEAR PARAFFINS IS ENHANCED BY THE PRESENCE IN THE FEED OF C9 AND C10 AROMATICS CONTAINING MULTI-METHYL OR ETHYL GROUPS ON THE BENZENE RING TOGETHER WITH A HIGH RATIO OF HYDROGEN TO HYDROCARBON, EVEN THOUGH BOTH AROMATICS AND HYDROGEN ARE PRODUCTS OF THE REACTION. THEREFORE, A VARIATION IN THE PROCESS ACCOMPLISHES DEHYDROCYCLIZATION OF C6 AND C7 LINEAR PARAFFINS IN AN UPSTREAM ZONE OF THE DEHYDROCYCLIZA TION PHASE AND UTILIZES THE HYDROGEN AND AROMATICS THEREIN PRODUCED WITH OR WITHOUT HYDROGEN AND AROMATICS PRODUCED IN THE HIGH PRESSURE NAPHTHENE AROMATIZATION PHASE TO ENHANCE DEHYDROCYCLIZATION OF C9 AND C10 PARAFFINS WHICH ARE SEPARATELY ADDED TO A DOWNSTREAM ZONE IN THE DEHYDROCYCLIZATION PHASE.

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