Staged catalyst addition for catalytic liquid phase oxidation of pseudocumene to trimellitic acid
    3.
    发明授权
    Staged catalyst addition for catalytic liquid phase oxidation of pseudocumene to trimellitic acid 失效
    标准催化剂添加剂对PSEUDOCUMENE对三叶酸的催化液相氧化

    公开(公告)号:US3683016A

    公开(公告)日:1972-08-08

    申请号:US3683016D

    申请日:1970-04-24

    CPC classification number: C07C51/265 C07C63/307

    Abstract: Reduced tendency for oxidation inhibition leading to formyl phthalic acids and methyl phthalic acids during liquid phase oxidation of 1,2,4-trimethylbenzene with molecular oxygen in the presence of acetic acid and catalysis provided by a source of bromine and staged use of two or more heavy metals is further reduced by staging addition of cobalt, manganese and cerium by maintaining a weight ratio of bromine to total metals above 1.0 in all stages and conducting the oxidation at a temperature in the range of 360*-440* F. with the last stage above 400* F. At the same time reduced oxidation of acetic acid to oxides of carbon and water and reduced requirements for total metal and bromine sources are achieved without sacrifice of reaction time or yield and quality of trimellitic acid.

    Abstract translation: 在乙酸存在下,用分子氧在1,2,4-三甲基苯的液相氧化期间氧化抑制的趋势导致甲酰邻苯二甲酸和甲基邻苯二甲酸,由溴源提供的催化作用,并分阶段使用两种或更多种 重金属进一步通过分级添加钴,锰和铈进一步减少,通过将溴与总金属的重量比保持在所有阶段高于1.0,并在360°-440°F的温度下进行氧化,最后 同时在不牺牲反应时间或偏苯三酸的产率和质量的情况下,将乙酸氧化成碳和水的氧化物,同时降低对总金属和溴源的需求。

    4.
    发明专利
    未知

    公开(公告)号:DE2119118C3

    公开(公告)日:1980-12-18

    申请号:DE2119118

    申请日:1971-04-20

    Abstract: Reduced tendency for oxidation inhibition leading to formyl phthalic acids and methyl phthalic acids during liquid phase oxidation of 1,2,4-trimethylbenzene with molecular oxygen in the presence of acetic acid and catalysis provided by a source of bromine and staged use of two or more heavy metals is further reduced by staging addition of cobalt, manganese and cerium by maintaining a weight ratio of bromine to total metals above 1.0 in all stages and conducting the oxidation at a temperature in the range of 360 DEG -440 DEG F. with the last stage above 400 DEG F. At the same time reduced oxidation of acetic acid to oxides of carbon and water and reduced requirements for total metal and bromine sources are achieved without sacrifice of reaction time or yield and quality of trimellitic acid.

    6.
    发明专利
    未知

    公开(公告)号:FR2090667A5

    公开(公告)日:1972-01-14

    申请号:FR7114642

    申请日:1971-04-23

    Abstract: Reduced tendency for oxidation inhibition leading to formyl phthalic acids and methyl phthalic acids during liquid phase oxidation of 1,2,4-trimethylbenzene with molecular oxygen in the presence of acetic acid and catalysis provided by a source of bromine and staged use of two or more heavy metals is further reduced by staging addition of cobalt, manganese and cerium by maintaining a weight ratio of bromine to total metals above 1.0 in all stages and conducting the oxidation at a temperature in the range of 360 DEG -440 DEG F. with the last stage above 400 DEG F. At the same time reduced oxidation of acetic acid to oxides of carbon and water and reduced requirements for total metal and bromine sources are achieved without sacrifice of reaction time or yield and quality of trimellitic acid.

    CATALYTIC OXIDATION PROCESS FOR PRODUCING TRIMELLITIC ACID

    公开(公告)号:GB1353482A

    公开(公告)日:1974-05-15

    申请号:GB1107371

    申请日:1971-04-23

    Abstract: 1353482 Trimellitic acid STANDARD OIL CO 23 April 1971 [24 April 1970] 11073/71 Heading C2C [Also in Division B1] Trimellitic acid is produced by subjecting pseudocumene in liquid phase to catalytic molecular oxygen oxidation in an oxidation medium comprising from 3À0 to 4À0 parts by weight of acetic acid per part by weight of pseudocumene and as catalyst, a combination of cobalt manganese, cerium and bromine sources, in which process the cobalt, manganese and cerium sources provide a total of from 0À2 to 0À4 weight per cent metals based on the amount of pseudocumene; the oxidation is conducted in a series of stages for each of which a substantially equal quantity of cerium is added to the oxidation medium and during each of which the weight of bromine (expressed as bromide ion) to total metal ions is from 1À5 : 1À0 to 5À0 : 1À0, the proportion of cerium ions to total metal ions is from 5 to 25 wt. per cent and the proportion of manganese ions to total metal ions is from 10 to 25 wt. per cent; all of the cobalt and from 10 to 25 wt. per cent of the manganese are added to the oxidation medium for the first stage; the remaining 75 to 90 wt. per cent of the manganese is added subsequently to the oxidation medium; the temperature in the last stage is upward from 400‹ F. and the temperature in the stage preceding the last stage is between 350‹ and 400‹ F. Examples are furnished.

    8.
    发明专利
    未知

    公开(公告)号:BE766239A

    公开(公告)日:1971-09-16

    申请号:BE766239

    申请日:1971-04-23

    Abstract: Reduced tendency for oxidation inhibition leading to formyl phthalic acids and methyl phthalic acids during liquid phase oxidation of 1,2,4-trimethylbenzene with molecular oxygen in the presence of acetic acid and catalysis provided by a source of bromine and staged use of two or more heavy metals is further reduced by staging addition of cobalt, manganese and cerium by maintaining a weight ratio of bromine to total metals above 1.0 in all stages and conducting the oxidation at a temperature in the range of 360 DEG -440 DEG F. with the last stage above 400 DEG F. At the same time reduced oxidation of acetic acid to oxides of carbon and water and reduced requirements for total metal and bromine sources are achieved without sacrifice of reaction time or yield and quality of trimellitic acid.

    9.
    发明专利
    未知

    公开(公告)号:DE2119118B2

    公开(公告)日:1980-04-24

    申请号:DE2119118

    申请日:1971-04-20

    Abstract: Reduced tendency for oxidation inhibition leading to formyl phthalic acids and methyl phthalic acids during liquid phase oxidation of 1,2,4-trimethylbenzene with molecular oxygen in the presence of acetic acid and catalysis provided by a source of bromine and staged use of two or more heavy metals is further reduced by staging addition of cobalt, manganese and cerium by maintaining a weight ratio of bromine to total metals above 1.0 in all stages and conducting the oxidation at a temperature in the range of 360 DEG -440 DEG F. with the last stage above 400 DEG F. At the same time reduced oxidation of acetic acid to oxides of carbon and water and reduced requirements for total metal and bromine sources are achieved without sacrifice of reaction time or yield and quality of trimellitic acid.

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