• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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    • 专利摘要:
    Process for continuous production of substantially anhydrous solutions of perpropionic acid in benzene. Aqueous hydrogen peroxide is first reacted with propionic acid in the presence of acid catalyst to form perpropionic acid and water (1). The perpropionic acid is extracted with benzene (5), to provide a benzene phase containing the perpropionic acid (11) and an aqueous raffinate (7). The benzene phase is subjected to an extraction with water (12) involving at least 3 stages, to remove hydrogen peroxide, and the resulting benzene extract (15) is subjected to azeotropic distillation (26) to provide the anhydrous solution (17). The aqueous raffinate, which contains hydrogen peroxide, is distilled to remove water (8) and the resulting concentrate is recycled (2) for use in the reaction (1).
    公开号:SU719497A3
    申请号:SU762351995
    申请日:1976-04-28
    公开日:1980-02-29
    发明作者:Прешер Гюнтер；Шрейер Герд；Вайберг Отто；Виртвейн Рольф；Вальдманн Гельмут；Зейферт Герман；Швердтель Вульф；Своденк Вольфганг
    申请人:Дойче Гольд-Унд Зильбер-Шайдеанштальт Формальс Ресслер (Фирма)；Байер Аг (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR RECOVERY OF HYDROGEN PEROXIDE
    which is fed to the last stage and withdrawn from the second stage. The proposed method consists in combining one-step cross-extraction with a two- or three-stage orotheat extraction. In the first stage, an apparatus such as a mixer-separator is used as an extractor, and any type of extractor can be used in the remaining stages. The extraction is carried out at a temperature from room temperature to 30 ° C. The initial mixture usually contains weight. %: 5-50 percarboxylic acid, 5-50 carboxylic acid, 10-70 organic solvent, 0.2-1 water and 0.2-1 hydrogen oxide.
    FIG. 1-4 schematically represent the proposed method, where I-III means the reaction stages.
    Example 1 (see Fig. 1). 74.27 kg / h mixture of the following composition, weight. %: 22.3 iadproiopic acid; 13.8 propnoic acid; 62.5 Beisol; 0.86 of water and 0.54 of hydrogen peroxide; through pipeline 1 it is fed to the first stage of extraction, to which 0.82 kg / h of water is supplied via pipeline 2, and 2.92 kg / h of mixture containing 99 via pipeline 3, 2 wt. % water and 0.8 wt. % hydrogen peroxide, the total amount of water is 5% by weight of the mixture. 3.97 kg / h of a mixture of the following composition, weight, is obtained as an extract. %: 34.1 supropropionic acid, 22.1 propnonic acid, 10.0 benzene, 29.9 water and 3.9 hydrogen skewers, which are removed through conduit 4. 74 kg / h of a mixture of the composition, wt. %: 20.64 nadnopnonovoy acid, 62.12 benzene, 4.18 water and 0.36 hydrogen peroxide, which is fed through line 5 to the second stage of extraction, from which 73.96 kg / h of refined product is withdrawn, weight. %: 20.65 nadponionic acid, 12.72 propnonic acid, 62.15 benzene, 4.18 water, n 0.30 neremni hydrogen, which, however, is supplied to pipeline b to the third stage of extraction, to which 0.93 kg is fed through pipeline 7 / h (1.25% by weight of the mix) water. From this stage, 3.64 kg / h of extract of the composition, weight, are withdrawn. %: 33.8, supropropionic acid, 21.4 pronnonic acid, 10.4 benzene, 32.5 water and 1.9 hydrogen peroxide, which is fed through line 8 to the second extraction stage, from which 9 is diverted through line 9, 68 kg / h of extract composition, weight. %: 33.4 nadpropionic acid, 21.3 propionic acid, 10.2 benzene, 32.0 water, and 3.1 hydrogen peroxide. 71.25 kg / h rafnnata discharged from the third stage of extraction through the pipeline 10, has a composition, weight. %: 19.7 supropropionic acid, 12.1 propnonic acid, 64.01 benzene, 4.0 water and 0.19 hydrogen peroxide. Extraction at all stages is carried out at a temperature of 28-30 ° C.
    Example 2 (see fng. 2). Example 1 is repeated, with the difference that non-current extraction is carried out in four stages.
    74.27 kg / h of the mixture specified in example 1, but pipeline 1 is fed to the first extraction stage, to which 0.82 kg / h of water is iodized to pipeline 2, and 2.92 kg / h is mixed via pipeline 3. The total amount of water is 5% by weight of the mixture. 4.24 kg / h of a mixture of the composition, weight, are obtained as an extract. %: 32.62 supropropionic acid, 21.00 nopionic acid, 9.43 beisol, 33.25 water and 4.00 hydrogen peroxide, which is diverted through conduit 4. 73 kg / h of a mixture, weight, is obtained as raffinate. %: 20.64 nadiropionic acid, 12.70 iropionic acid, 62.42 benzene, 39.0 water and 0.34 hydrogen ireoxide, which is fed through conduit 5 to the second extraction stage, to which, but conduit 11, serves 3.81 kg / h mixture composition, weight. %: 34.13 nadpropiopic acid, 9.97 benzene, 30.97 water and 2.62 hydrogen peroxide.
    4.13 kg / h are obtained as an extract.
    %: 34,87 nadironionosmes composition, weight. howl acid, 24,21 nropionic acid.
    9.20 benzene, 28.57 water and 3.15 non-hydrogen oxide, which is diverted through conduit 9. 73.40 kg / h of a mixture of the composition, wt. %: 20.54 suprapropionic acid, 12.56 propnone acid, 62.70 benzene, 3.90 water and 0.30 hydrogen peroxide, which is fed through conduit 6 to the third extraccin herd, which is served by conduit 12 to 3.64 kg / h extract obtained in the fourth stage of extraction. This extract has a composition by weight. %: 33.79 supropropionic acid, 21.43 propnonic acid, 10.44 benzene, 32.44 water and 1.90 non-oxygen hydrogen. From the third stage of extraction, 73.23 kg / h of raffinate composition, weight, were withdrawn. %: 20.5 supropropionic acid, 12.5 propionic acid, 62.84 benzene, 3.90 water and 0.26 hydrogen peroxide, which is fed through conduit 13 to the fourth extraction stage, to which 0.93 kg is fed via conduit 14 / h of water (1.25% by weight of the mixture). As a raffinate receive 70,52 kg / h of the mixture composition, weight. %: 19.54 supranionic acid, 11.87 propionic acid, 64.72 benzene, 3.70 water, and 0.17 hydrogen peroxide, which is discharged through pipeline 15.
    Extraction in all herds was performed at room temperature.
    Example 3 (see Fig. 3). The process is carried out similarly to example 1. 74.27 kg / h of the mixture of the composition indicated in example 1, via pipeline 1, is fed to the first extraction, to which 2.30 kg / h of water is supplied via pipeline 2, and 2.92 kg via pipeline 3 / h mixture specified in example 1 composition. The total amount of water is 7% by weight of the mixture.
    6.67 kg / h are obtained as an extract.
    mixture of composition, wt. %: 31.36 nadpropionic acid, 18.59 propionic acid, 4.33 benzene, 41.8 water and 3.92 hydrogen peroxide, which is removed via conduit 4. 72.28 kg / h of a mixture of the composition are obtained as raffipate, weight. %: 19.97 padpropionic acid, 12.39 propionic acid, 63.46 benzene, 3.83 water and 0.35 hydrogen peroxide, which is fed through conduit 5 to the second stage of extraction, which also serves 0.94 kg / h extract obtained in the third stage of extraction. The extract supplied through the pipeline 8, has a composition, weight. %: 37.46 nadpropanoic acid, 22.07 propionic acid, 10.03 benzene, 28.29 water, and 2.15 hydrogen peroxide. From the second stage of extraction, through pipeline 9, 0.96 kg / h of the mixture of the composition, weight, is withdrawn. %: 37.51 nadpropionic acid, 22.63 propionic acid, 10.0 benzene, 26.38 water and 3.48 hydrogen peroxide. 72.26 kg / h are obtained as a raffinate. %: 20.0 nadpropionic acid, 12.38 peronic acid, 63.41 benzene, 3.93 water and 0.28 hydrogen peroxide, which is fed through conduit 6 to the third extraction herd, to which 0.37 kilos are supplied via conduit 7 / h of water (0.5% by weight of the initial mixture). 72.18 kg / h of a mixture of the composition, weight, are obtained as a raffinate. %: 19.62 nadpropionic acid, 12.20 propiopic acid, 63.85 benzene, 4.15 water, and 0.18 hydrogen peroxide.
    Extraction at all stages is carried out at room temperature.
    Example. 4 (see Fig. 4). The process is carried out analogously to example 2. 74.27 kg / h of the mixture of the composition indicated in Nimer 1 is supplied via pipeline 1 to the first stage, to which 2.24 kg / h of the composition indicated in Example 1 (quantity of water 3% by weight of the mixture). After extraction at 28-30 ° C, pipeline 5 withdraws 76.51 kg / h of the mixture of the composition by weight. %: 21.64 nopronionic acid, 13.40 propionic acid, 60.60 benzene, 3.80 water and 0.56 hydrogen peroxide, which is fed to the second stage of extraction, which is dried at the same temperature as the first stage of extraction . At the second stage of extraction through the pipeline 11 serves 5.29 kg / h of the mixture of the composition, weight. %: 35.34 n-propionic acid, 23.15 propionic acid, 10.0 benzene, 28.92 water and 2.89 hydrogen peroxide. 5.46 kg / h of a mixture of the composition, wt. %: 36.55 nadpropionic acid, 22.15 nropionic acid, 9.00 benzene, 28.10 water and 5.20 hydrogen peroxide, which is discharged through line 9.
    As a raffinate, 76.34 kg / h of a mixture of composition, wt.%: 21.62 perpropionic acid, 13.57 perionic acid, 60.65 benzene, 3.88 water and 0.28 hydrogen peroxide, which is supplied to pipeline 6, is obtained in the third extraction stage, which is carried out at the same temperature as the first extraction stage. At the third stage of extraction, 5.12 kg / h of the extract obtained in the fourth stage of extraction are also fed. This extract, which is fed by pipeline J2, has a composition, weight. % 35.74 perpropionic acid, 22.67 peronic acid, 10.65 benzene, 29.89 water and 1.05 hydrogen peroxide. As the raffinate of the third stage of extraction, 76.17 kg / h of the mixture of the composition, weight, are obtained. %: 21.52 nadproionic acid, 13.55 propionic acid, 60.87 benzene, 13.82 water and 0.24 hydrogen peroxide, which is fed through conduit 13 to the fourth extraction stage, which is carried out at the same temperature as first stage of extraction. At the fourth stage of extraction through the pipeline 14 serves 1,49 kg / h of water (2% by weight of the initial mixture). From this stage of extraction, through pipeline 15, 72.54 kg / h of a mixture of the composition, weight, are withdrawn. %: 20.22 nadpropionic acid, 12.45 propiopic acid, 63.15 benzene, 4.00 water and 0.18 hydrogen peroxide.
    Prnmer 5 (comparative). Example 1 is repeated, with the difference that 74.27 kg / h of the mixture in Example 1 of composition is countercurrently extracted with 3.27 kg / h of water. At the same time, as a raffipath, an offal of 73.86 kg / h of a mixture of the composition, weight. %; 21.55 nadpropioic acid, 13.05 nropionic acid, 61.90 benzene, .3.07 water and 0.43 (i.e., 0.3176 kg / h) hydrogen peroxide, and as an extract 3.68 kg / h mixture composition, wt. %: 16.50 padpropionic acid, 16.50 propionic acid, 19.3 benzene, 45.2 water and 2.5 hydrogen peroxide. The recovery rate of NaOZ is 29.3%, based on a total of 0.423 kg / h.
    Example 6 (comparable) Example 1 is repeated, with the difference that 3.27 kg / h of water is injected into the third stage of extraction, which is passed through three stages in countercurrent to the original mixture. From the first stage of extraction, 7.04 kg / h of extract containing, wt. %: 43.42 nadpropononic acid, 28.10 nioionic acid, 10.52 benzene, 16.22 water and 1.84 hydrogen peroxide, and from the third stage of extraction 70.50 kg / h of raffinate composition, weight. %: 19.16 nadpropiopic acid, 11.72 pro-ionic acid, 64.80 benzene, 3.94 water and 0.38 hydrogen peroxide.
    The table shows the degree of hydrogen peroxide recovery,%, taking into account the fact that the amount of hydrogen peroxide in the initial mixture is taken as 100%.
    As can be seen from the table, the degree of hydrogen peroxide recovery is more than twice the known one.
    In addition, the use of water in an amount of less than 3% weight. Ia of the first stage and in the amount of less than 0.5 weight. % in the remaining stages leads to a decrease in the recovery rate of hydrogen peroxide by 35–40%, and exceeding the specified limits does not provide a better degree of recovery.
    权利要求:
    Claims (2)
    [1]
    1. Vylozheina for the Federal Republic of Germany No. 1917032, cl. 12o II, publ. 1970.
    [2]
    2. Published in the Federal Republic of Germany No. 2141156, cl. From 07C 73/10, published. 1974.
    3 Laid for Germany №2262970, cl. From 07C 73/10, oublik. 1974 (prototype).
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    法律状态:
    优先权:
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