Method for the preparation of dialkalioxydiacetate
    1.
    发明授权
    Method for the preparation of dialkalioxydiacetate 失效
    二氯二乙酸二乙酯的制备方法

    公开(公告)号:US3890381A

    公开(公告)日:1975-06-17

    申请号:US42377873

    申请日:1973-12-11

    CPC classification number: C07C51/235 C07C59/305

    Abstract: A method for preparing a dialkalioxydiacetate by contacting diethylene glycol with a gas containing molecular oxygen in the presence of water, an alkaline substance and a catalyst. The catalyst is composed of at least one of palladium, platinum, rhodium, ruthenium, rhenium, osmium, iridium and the oxides thereof.

    Abstract translation: 一种通过在水,碱性物质和催化剂存在下使二甘醇与含有分子氧的气体接触来制备二烷二酸二乙酸酯的方法。 催化剂由钯,铂,铑,钌,铼,锇,铱及其氧化物中的至少一种构成。

    3.
    发明专利
    未知

    公开(公告)号:DE3777571D1

    公开(公告)日:1992-04-23

    申请号:DE3777571

    申请日:1987-06-25

    Abstract: Improved process for producing chlorine molecules comprises oxidn. of hydrochloric acid with molecular oxygen. This oxidn. process is carried out in the presence of a catalyst, and chromium oxide. The chromium oxide is prepd. by (1) chromium oxide is carried on a silicon oxide carrier which has a porosity of 0.3-1.8 cc/g, with amt. of carried chromium oxide evaluated as chromia, of 20-90 wt.%, (2) carried chromium oxide is heat treated at 450-700 deg.C. The chromium oxide catalyst is obtd. by contacting aq.soln. of chromate anhydride or chromium salt with silicon oxide, and then drying and heat treating. The oxidn. reaction is carried out in a flow process at a temp. 350-430 deg.C in the presence of molecular oxygen. The molecular ratio of oxygen to HCl lies between 0.25-5 and the flow rate of HCl is 200-1800 Nl/Kg catalyst/hour. The radius of the porous holes in the silicon oxide carrier lies between 20 and 300 Angstroms.

    PROCESS FOR PRODUCING CHLORINE
    4.
    发明专利

    公开(公告)号:AU7583187A

    公开(公告)日:1988-01-29

    申请号:AU7583187

    申请日:1987-06-25

    Abstract: Improved process for producing chlorine molecules comprises oxidn. of hydrochloric acid with molecular oxygen. This oxidn. process is carried out in the presence of a catalyst, and chromium oxide. The chromium oxide is prepd. by (1) chromium oxide is carried on a silicon oxide carrier which has a porosity of 0.3-1.8 cc/g, with amt. of carried chromium oxide evaluated as chromia, of 20-90 wt.%, (2) carried chromium oxide is heat treated at 450-700 deg.C. The chromium oxide catalyst is obtd. by contacting aq.soln. of chromate anhydride or chromium salt with silicon oxide, and then drying and heat treating. The oxidn. reaction is carried out in a flow process at a temp. 350-430 deg.C in the presence of molecular oxygen. The molecular ratio of oxygen to HCl lies between 0.25-5 and the flow rate of HCl is 200-1800 Nl/Kg catalyst/hour. The radius of the porous holes in the silicon oxide carrier lies between 20 and 300 Angstroms.

    7.
    发明专利
    未知

    公开(公告)号:DE69001160D1

    公开(公告)日:1993-04-29

    申请号:DE69001160

    申请日:1990-07-16

    Abstract: Methanol is decomposed in the presence of a catalyst containing chromium oxide and zinc oxide as main components and containing a compound of at least one element selected from alkali metals, alkali earth metals and lanthanides, while contents of iron and nickel in the catalyst are each maintained at 0.5% by weight or less. This process is characterised by (1) being excellent in stability at high temperatures, (2) preventing the catalyst from deteriorating, (3) inhibiting the production of by-products, and (4) obtaining a gas in which the CO/H2 ratio is high.

    PROCESS FOR PRODUCING CATALYST FOR OXIDIZING HYDROGEN-CHLORIDE

    公开(公告)号:HU201495B

    公开(公告)日:1990-11-28

    申请号:HU342987

    申请日:1987-06-25

    Abstract: Improved process for producing chlorine molecules comprises oxidn. of hydrochloric acid with molecular oxygen. This oxidn. process is carried out in the presence of a catalyst, and chromium oxide. The chromium oxide is prepd. by (1) chromium oxide is carried on a silicon oxide carrier which has a porosity of 0.3-1.8 cc/g, with amt. of carried chromium oxide evaluated as chromia, of 20-90 wt.%, (2) carried chromium oxide is heat treated at 450-700 deg.C. The chromium oxide catalyst is obtd. by contacting aq.soln. of chromate anhydride or chromium salt with silicon oxide, and then drying and heat treating. The oxidn. reaction is carried out in a flow process at a temp. 350-430 deg.C in the presence of molecular oxygen. The molecular ratio of oxygen to HCl lies between 0.25-5 and the flow rate of HCl is 200-1800 Nl/Kg catalyst/hour. The radius of the porous holes in the silicon oxide carrier lies between 20 and 300 Angstroms.

    9.
    发明专利
    未知

    公开(公告)号:DE69001160T2

    公开(公告)日:1993-09-30

    申请号:DE69001160

    申请日:1990-07-16

    Abstract: Methanol is decomposed in the presence of a catalyst containing chromium oxide and zinc oxide as main components and containing a compound of at least one element selected from alkali metals, alkali earth metals and lanthanides, while contents of iron and nickel in the catalyst are each maintained at 0.5% by weight or less. This process is characterised by (1) being excellent in stability at high temperatures, (2) preventing the catalyst from deteriorating, (3) inhibiting the production of by-products, and (4) obtaining a gas in which the CO/H2 ratio is high.

    MANUFACTURING PROCESS OF CHLORINE
    10.
    发明专利

    公开(公告)号:CA1283771C

    公开(公告)日:1991-05-07

    申请号:CA541275

    申请日:1987-07-03

    Abstract: In the process of producing chlorine by oxidizing hydrogen chloride with molecular oxygen, activity of the catalyst can be maintained for a long period with a high conversion ratio under high space velocity of gaseous raw materials without using additives as conventional methods, in the presence of a crystalline chromic oxide catalyst obtained by supporting relatively large amount of chromic oxide on a silicon oxide carrier having a specified pore volume.

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