Dihalogenation of 1,4-substituted alkylcyclo-hexanes
    43.
    发明授权
    Dihalogenation of 1,4-substituted alkylcyclo-hexanes 失效
    1,4-取代的烷基胆碱的二氢化

    公开(公告)号:US3763249A

    公开(公告)日:1973-10-02

    申请号:US3763249D

    申请日:1971-03-31

    Inventor: SCHNEIDER A

    CPC classification number: C07C17/10 C07C23/10

    Abstract: ALKYLCYCLOHEXANES HAVING 2-6 UNBRANCHED ALKYL SUBSTITUENTS INCLUDING A SINGLE SUBSTITUENT AT EACH OF THE 1- AND 4-POSITIONS ARE DICHLORINATED, DIBROMINATED OR DIFLUORINATED AT THE 1,4-POSITIONS BY REACTION WITH A C4-C5 TERTIARY ALKYL CHLORIDE, BROMIDE OR FLUORIDE. THE REACTION IS EFFECTED BT CONTACTING A MIXTURE OF THE REACTANTS, CONTAINING A LARGE MOLAR EXCESS (>2:1) OF THE TERTIARY ALKYL HALIDE, WITH 90-100% SULFURIC ACID OR 90-100% HYDROFLUORIC ACID AT A TEMPERATURE BELOW 50* C., PREFERABLY 0-30* C. THE RECOVERED 1,4 -DIHALOALKYLCYCLOHEXANES HAVE UTILITY AS INTERMEDIATES FOR PREPARING DIFUNCTIONAL DERIVATIVES, E.G. DIACIDS, DIALCOHOLS OR DIAMIDES, WHICH ARE USEFUL AS MONOMERS IN POLYMER MANUFACTURE.

    Use of thermal regenerator pair in sodium recovery process
    44.
    发明授权
    Use of thermal regenerator pair in sodium recovery process 失效
    热再生器对在钠回收过程中的应用

    公开(公告)号:US3759703A

    公开(公告)日:1973-09-18

    申请号:US3759703D

    申请日:1971-11-15

    Inventor: CHONG V

    CPC classification number: C22B26/10

    Abstract: IN A SODIUM GENERATION SYSTEM WHERE SODIUM CARBONATE AND COKE ARE REACTED TO GENERATE SODIUM, THE IMPROVEMENT COMPRISING THE CYCLIC OPERATION OF A PAIR OF THERMAL REGENERATORS WHEREBY IN ONE HALF-CYCLE THE CO2 OFF GAS FROM THE SODIUM GENERATOR IS PASSED THROUGH ONE OF SAID REGENERATORS HAVING AN INTERNAL TEMPERATURE BELOW THE FUSION POINT OF SODIUM CARBONATE THEREBY TRAPPING ANY VOLATILIZED CARBONATE IN SAID REGENERATOR, AND IN A SECOND HALF-CYCLE, CARBON MONOXIDE IS BURNED IN SAID REGENERATOR WHEREBY THE SODIUM COMPOUNDS TRAPPED IN SAID REGENERATOR ARE VAPORIZED AND RETURNED WITH THE EXITING GASES TO SAID SODIUM GENERATION SYSTEM.

    Alkyladamantane diamine
    45.
    发明授权
    Alkyladamantane diamine 失效
    亚胺基二胺

    公开(公告)号:US3748359A

    公开(公告)日:1973-07-24

    申请号:US3748359D

    申请日:1971-10-22

    Inventor: THOMPSON R

    CPC classification number: C07C49/323

    Abstract: THIS INVENTION RELATES TO A ALKYLADAMANTANE DIAMINE; NAMELY, 1,3 - DIMETHYLENEAMINE-5,7-DIMETHYLADAMANTANE, AND TO THE PREPARATION OF IT AND ITS HOMOLOGUES FROM AN ALKYLADAMANTANE DIACID THE PREPARATION STARTS WITH THE CHLORINATION OF THE ALKYLADAMANTANE DIACID WHICH IS FOLLOWED BY THE AMINDATION OF THE RESULTING DIACID CHLORIDE, WHICH IS TURN IS FOLLOWED BY THE DEHYDRATION OF THE RESULTING DIAMIDE AND ENDS WITH THE HYDROGENATION OF THE RESULTING DINITRILE. THE NAMED DIAMINE HAS THE FOLLOWING STRUCTURAL FORMULA:

    3,7-DI(NH2-CH2-),1,5-DI(CH3-)ADAMANTANE

    AND IS A WHITE, CRYSTALLINE SOLID USEFUL IN VARIOUS APPLICATIONS, FOR EXAMPLE CORROSION INHIBITOR, CHEMICAL INTERMEDIATE, AND A COMPONENT OF USEFUL POLYMERS.

    Stabilization of coal
    46.
    发明授权
    Stabilization of coal 失效
    煤炭稳定化

    公开(公告)号:US3723079A

    公开(公告)日:1973-03-27

    申请号:US3723079D

    申请日:1971-07-23

    Inventor: SEITZER W

    CPC classification number: C10L9/06

    Abstract: A process for stabilizing dried lignitic and subbituminous coal against spontaneous combustion which comprises treating said dried coal at about 175* to about 225* C. with oxygen in an amount of from about 0.5 percent to about 8 percent by weight of said coal and rehydrating the oxygen treated coal with water in an amount of from about 1.5 percent to about 6 percent by weight of said oxygen treated coal.

    Abstract translation: 一种用于稳定干燥的褐煤和次烟煤对抗自发燃烧的方法,其包括在约175至约225℃下处理所述干燥的煤,其量为所述煤重量的约0.5%至约8%,并将 经氧处理的煤与水的量为所述氧处理煤的约1.5重量%至约6重量%。

    Microbial production of novel hydroxyphenyl ketobutyric acids
    48.
    发明授权
    Microbial production of novel hydroxyphenyl ketobutyric acids 失效
    新型羟基苯乙酮的微生物生产

    公开(公告)号:US3676299A

    公开(公告)日:1972-07-11

    申请号:US3676299D

    申请日:1970-10-22

    Abstract: NOVEL HYDROXYPHENYLKETOBUTYRIC ACIDS HAVING THE STRUCTURAL FORMULA:

    (2-HO,6-R3,R1,R2-PHENYL)-(CH2)2-CO-COOH

    WHEREIN R1 AN R2 ARE HYDROGEN OR LOWER ALKYL GROUPS HAVING FROM ONE TO THREE CARBON ATOMS; R3 IS HYDROGEN, AND WHEREIN R1 AND R2 MAY BE THE SAME OR DIFFERENT, ARE PREPARED BY SUBJECTING NAPHTHALENE OR ALKYL-SUBSTITUTED NAPHTHALENES HAVING THE STRUCTURAL FORMULA:

    1-R3,R1,R2-NAPHTHALENE

    WHEREIN R1, R2 AND R3 ARE AS DEFINED ABOVE, TO THE OXIDIZING ACTIVITY OF THE MICROOGRANISMS NOCARDIA COELIACA, ATCC NO. 21,146, NOCARDIA NOV. SP., ATCC NO. 21,145, OR STREPTOMYCES SPECIES, ATCC NO. 21,147.

    Process for preparation of isomers of 1-cyclohexyl-1,3,3-trimethylhydrindane
    49.
    发明授权
    Process for preparation of isomers of 1-cyclohexyl-1,3,3-trimethylhydrindane 失效
    1-环己基-1,3,3-三甲基环己烷的异构体的制备方法

    公开(公告)号:US3929923A

    公开(公告)日:1975-12-30

    申请号:US21833872

    申请日:1972-01-17

    Abstract: A process is disclosed for the hydrogenation of 1-phenyl-1,3,3trimethylindane to prepare selected isomers. For example 4,9-cis, 1-cyclohexyl-1,3,3-trimethylhydrindane, a fluid with improved tractive properties, can be prepared using a catalyst containing nickel, palladium or rhodium at a hydrogen pressure in the range of 600 to 1500 p.s.i.g., and a temperature substantially in the range of 200*C. to 225*C.

    Abstract translation: 公开了1-苯基-1,3,3-三甲基茚满氢化制备选择的异构体的方法。 例如4,9-顺式,1-环己基-1,3,3-三甲基环己烷,具有改善的牵引性能的流体可以使用含有镍,钯或铑的催化剂在600至1500的氢气压力下制备 psig,温度基本上在200〜225℃的范围内。

    Dy zeolite hydrocarbon conversion catalyst
    50.
    发明授权
    Dy zeolite hydrocarbon conversion catalyst 失效
    Dy沸石烃转化催化剂

    公开(公告)号:US3914383A

    公开(公告)日:1975-10-21

    申请号:US28191072

    申请日:1972-08-18

    Abstract: A Dy-alumino-silicate catalyst, useful for hydrocarbon conversion reactions, is chemically characterized by the empirical formula Mx(A102)x(SiO2)y.(H2O)z, where x, y and z are integers, the ratio x:y being usually from 1.0 to 0.2 and where at least 25% (and preferably more than 40%) of the negative charge associated with the aluminum of the alumino-silicate framework is satisfied by a cation of Dy or a cation of an oxide or a hydroxide of Dy. Preferably, upon ignition analysis the catalyst will evolve from 1 to 6 molecules of water (typically 1.5-2.5molecules) for each atom of Dy in the catalyst. Typically the negative charge associated with the zeolite framework is not completely satisfied by cations containing Dy and the balance of cations necessary for electronic equivalency comprise H or cations of metals, metal oxides or metal hydroxides. The zeolite also contains less than one alkali metal cation for every four atoms of aluminum in the framework. The zeolite can be amorphous, but preferably is at least partially crystalline and can adsorb benzene.

    Abstract translation: 用于烃转化反应的Dy-铝硅酸盐催化剂的化学特征在于经验式Mx(A102)x(SiO2)y。(H2O)z,其中x,y和z是整数,x:y 通常为1.0至0.2,并且通过Dy阳离子或氧化物或氢氧化物的阳离子满足与铝硅酸盐骨架的铝相关的负电荷的至少25%(优选大于40%) 的Dy。 优选地,在点燃分析时,对于催化剂中的每个Dy原子,催化剂将从1至6分子的水分(通常为1.5-2.5分子)放出。 通常,与沸石骨架相关的负电荷不完全满足含有Dy的阳离子,电子当量所需的阳离子余量包含H +或金属,金属氧化物或金属氢氧化物的阳离子。 沸石在框架中每四个铝原子也含有不到一个碱金属阳离子。 沸石可以是无定形的,但优选至少部分结晶并且可以吸附苯。

Patent Agency Ranking