• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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  • 引用文献
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    • 专利摘要:

    公开号:SU990078A3
    申请号:SU792797790
    申请日:1979-08-14
    公开日:1983-01-15
    发明作者:Кеннен Альфред；Коссвиг Курт；Винхефер Эккехард
    申请人:Хемише Верке Хюльс Аг (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR CLEANING CHLORINE HYDROGEN FROM BROMIDE HYDROGEN
    The invention relates to the purification of hydrogen halide, in particular to a method for purifying hydrogen chloride from hydrogen bromide. five
    A known method for the purification of hydrogen chloride from hydrogen bromide is that contaminated bromists with hydrogen chloride are exposed to a reaction of JO with chlorine at room or elevated temperature, followed by separation of the bromine formed. an excess of chlorine and purified hydrogen chloride, and the yield of that hydrogen chlorine jj is up to 99% Ll}.
    The disadvantage of this method is that the degree of purification of hydrogen chloride does not exceed 90%.
    The purpose of the invention is to increase the degree of purification of hydrogen chloride.
    This goal is achieved by the fact that according to the method of purifying hydrogen chloride from hydrogen bromide, which includes treating hydrochloric acid 25 with a reagent and separating the mixture obtained, an amine solution in an organic solvent and separation are used as a reagent. the resulting mixture is carried out by 30
    heat treating it at SO-ZOO C, separating the hydrogen chloride, treating the remaining products with an alkali metal hydroxide or carbonate or calcium hydroxide and sequentially separating the amine and alkali metal or calcium bromide. Trialkylamine, M-aryl-M, N-dialkylamine, N, N-diapyl-N-alkyl, N-alkyl-N-arylamine or N-alkylarylamine containing 14-36 carbon atoms is used as the amine.
    The drawing shows schematically an installation for the continuous implementation of the proposed method.
    In consistently included ab-. sorption columns 1 and 2 from the tank 3 through the pipeline 4 serves a solution of amine in an organic solvent. In addition, hydrogen chloride contaminated with hydrogen bromide is fed through line 5 to column 1. The amine solution is then exothermically saturated to form hydrochloride and amine hydrobromide. In the process of saturation, carried out at atmospheric pressure, the temperature does not exceed. After detection of hydrogen chloride free from hydrogen bromide discharged through line 6, the supply of initial hydrogen chloride to column 1 is stopped, and the process of saturation of the amine solution with initial x-porous hydrogen is repeated in column 2. After stopping the supply of initial hydrogen chloride the contents of columns 1 or 2 through conduit 7 are fed to heat treatment at SO-ZOO C into column 8, resulting in accumulation of hydrogen chloride discharged through conduit 9, after cooling, the solution containing more amine hydrobromide, the pipeline 10 is fed to the mixer 11, in which the solution is treated with hydroxide or alkali metal carbonate sludge calcium hydroxide, supplied as an aqueous solution through the pipeline 12. Upon completion of treatment, passed at 20-50 ° C and atmospheric pressure for not more than 30 minutes, the contents of the mixer 11 is supplied via pipe 13 to a tank 14, where the mixture is divided into an aqueous phase containing an alkali metal bromide and an organic phase containing the starting amine. The aqueous phase is withdrawn via conduit 15, and the organic phase via conduit 16 is fed to column 17 to be removed from decomposition products. on, for example, aluminum oxide, and then through the pipeline 18 recycle to the container 3. P p and me er1. In a 1/2-liter round-bottomed flask with a magnetic stirrer, equipped with a 30 cm long column filled with Raschig rings and a reflux condenser, a mixture of 86.3 g of tri-2-ethylhexyls (222.4 mmol), 6.3 g of bromide hydrogen (77.8 mmolv) and 10.5 g of hydrogen chloride (288.1 mmol) in 100 xylene and heated to 140 s. After 5 hours in two collections containing 200 ml 1 n. The amount of hydrogen chloride, which is 287.5 mmol (99.7%), is determined titrimetrically using sodium hydroxide solution. moreover, the purity of hydrogen chloride is 100% (according to x-ray fluorescence). From the product care 130/5, 0 NaOH
    I
    A 180 / 3.5 KOH
    I I
    B
    99/100
    96 96 98/100 from the bottom of the column, xylene is removed under a vacuum created with the help of a water jet pump, and residual amounts of hydrogen chloride and hydrogen bromide are determined by X-ray fluorescence. The hydrogen bromide content is 6.8% (calculated, 6.8%). By treating the residue with an aqueous solution of sodium hydroxide at 35 ° C, the hydrogen bromide is separated in an amount of 95%. Example 2. Example 1 is repeated, with the difference that 200 g of hexachlorobenzene are used as the solvent and the mixture is heated to 270 ° C. After 3.5 hours, the collections contain 286.9 mmol (99.6%) of 100% pure hydrogen chloride. 95.5% of the hydrogen bromide is separated from the residue by treatment with an aqueous solution of sodium hydroxide. Example 3; Example 1 is repeated with the difference that the mixture is heated to. After 2 hours, the collections contain 284.7 1 1 mol (98.8%) of hydrogen chloride with a purity of 100%. 92.5% of the hydrogen bromide is separated from the residue by treatment with an aqueous solution of sodium hydroxide. Example 4. Example 1 is repeated with the difference that the mixture is heated to 100 ° C. After 8 hours, the collections contain 278.3 mmol (96.6%) of hydrogen chloride. 89% of the hydrogen bromide is separated from the residue by treatment with an aqueous solution of sodium hydroxide. Example 5-38. Example 1 is repeated with the difference that 0.5 mol of gaseous hydrogen chloride contaminated with 0.005 mol of hydrogen bromide is fed into a mixture of 0.75 mmol of amine and 200 g of solvent. The resulting mixture is subjected to heat treatment, and the residue is treated with an aqueous solution of alkali. The amount of trapped hydrogen in the collections: hydrogen sulphide and separated hydrogen bromide is determined by titrimetric method. Amine, solvent, “process parameters and results are tabulated.
    Continuation of the tables
    "From the source
    Table continuation,
    In examples 5-8, alkali treatment is carried out at, in example 9 - at, in examples 10,11,19,21,25,31 and 32 - at, and in the rest of the examples - at.
    Formula inventions
    权利要求:
    Claims (2)
    [1]
    1. A method of purifying hydrogen chloride from hydrogen bromide, which includes treating hydrogen chloride with a reagent and separating the mixture obtained, characterized in that, in order to improve the degree of purification of hydrogen chloride, an amine solution in an organic solvent is used as a reagent and the resulting mixture is separated by heat treatment at 100 ° C, separation of hydrogen chloride, treatment of the remaining products with an alkali metal hydroxide or carbonate or calcium hydroxide and sequential separation tim amine and
    alkali metal or calcium.
    [2]
    2. The method according to p. 1, characterized in that in the quality of the amine use trigshilamine, G-aryl-M, M
    -dialkylamine, N, N-diaryl-alkyl, M-alkyl-M-arylsilon or N-alkylarylamine, the content of 14-36 carbon atoms.
    Information sources,
    taken into account in the examination
    1. The patent of Israel 34481, cl. From 01 to 7/00, published. 1973 (prototype).
    -IS
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    同族专利:
    公开号 | 公开日
    EP0008330A1|1980-03-05|
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    GB2030554B|1982-09-22|
    NL7906300A|1980-02-25|
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    FR2434115A1|1980-03-21|
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    引用文献:
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    DE873994C|1942-01-11|1953-04-20|Basf Ag|Process for the production of hydrogen halide solutions|
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    US2520947A|1946-04-08|1950-09-05|Phillips Petroleum Co|Recovery of hydrogen halides|
    US3210913A|1962-05-09|1965-10-12|Du Pont|Method for the separation of cof and hci|
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    US3445188A|1967-04-18|1969-05-20|Monsanto Co|Preparation of hydrogen bromide|
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    US3536593A|1968-09-25|1970-10-27|Gulf Research Development Co|Process for separating hydrocarbons from amines by conversion to amine salts and azeotrope distillation|
    DE2633640C3|1976-07-27|1979-03-15|Chemische Werke Huels Ag, 4370 Marl|Process for the production of gaseous hydrogen chloride from dilute aqueous hydrochloric acid|
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    JPH055903B2|1987-08-26|1993-01-25|Nitsuko Kyoseki Kk|
    US4830846A|1988-01-29|1989-05-16|The Dow Chemical Company|Separation process for anhydrous HCl and HBr by thermal cleavage|
    NO179243B1|1994-06-03|1996-09-23|Polymers Holding As|Process for removing unwanted color from hydrochloric acid, and using hydroxylamine hydrochloride to remove unwanted color from hydrochloric acid|
    JP2875480B2|1994-09-14|1999-03-31|日本エア・リキード株式会社|High-purity hydrogen bromide purification method and apparatus|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2836580A|DE2836580C3|1978-08-21|1978-08-21|Process for the separation of hydrogen chloride and hydrogen bromide|
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