• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Die Erfindung betrifft ein Katalysatorgemisch, bestehend aus wasserfreiem Eisen-III-chlorid sowie einer weiteren Gemischkomponente, zur Herstellung von 1,2-Dichlorethan durch Reaktion von Ethylen mit Chlor in einem Lösungsmittel bei Normal- oder Überdruck, welches dadurch gekennzeichnet ist, daß die weitere Gemischkomponente eine in Bezug auf die Eisen-III-chlorid-Menge etwa äquivalente Menge einer Stickstoffbase oder ein Salz dieser Base ist.
    公开号:SU1250165A3
    申请号:SU823520355
    申请日:1982-12-06
    公开日:1986-08-07
    发明作者:Хундек Йоахим；Шольц Харальд；Хеннен Ханс
    申请人:Хехст Аг (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to the field of chlorination catalysts, in particular catalysts for the continuous production of 1,2-dichloroethane by the reaction of ethylene with chlorine.
    The purpose of the invention is to reduce corrosion and increase the selectivity of the catalyst. PRI me R 1. In a loop reactor with a capacity of about 2 liters, put 2.0 kg of 1,2-dichloroethane and 4 g of anhydrous iron (III) chloride. The mixture at 20 ° C is injected with hydrogen chloride. The upstream part of the reactor loop contains a filler layer. Under the filler layer there are pipes for feeding ethylene, chlorine and air, through which chlorine, ethylene and air are supplied in quantities of 60, 60 and 15 liters per hour, respectively. 0.42 g of ammonia is added to ethylene over 10 hours. By neutralization, an appropriate amount of ammonium chloride is formed in the reaction mixture. The molar ratio of iron (III) to ammonium chloride is 1: 1. The reaction liquid in the reaction system circulates according to the principle of the Mammut pump and, at the same time, the catalyst mixture is simultaneously suspended in the liquid phase. During the reaction in the reaction mixture, the reaction temperature is maintained at 77 C.
    J In a cooler located above the reactor, dichloroethane vapor is condensed out of the reactor, and then the corresponding part of the condensate is separated and removed by a condensation element, while the excess condensate is returned to the reaction zone. With the help of a low-temperature trap, another part of dichloroethane is separated from gaseous wastes consisting mainly of inert gases. After a continuous process over several days, the catalyst mixture continues to dissolve in the reaction liquid, and the colorimetric determination of the iron content in the reaction liquid gives an iron (III) chloride content of about 0.12% by weight.
    The hourly amount of 1,2-dichloroethane produced is 263 g. The process is continuously carried out for several weeks.
    Analysis of the product A produced in the condenser, respectively
    2 liquids in after finishing gives the following results,
    Product A Product B
    0.002 0.002
    1,2-EDC 99.90 1,1,2-ETC 0.08
    HC1
    Other
    0,005 0,01
    99.72 0.24
    0.04
    EDC - 1,2 dichloroethane; ETC - 1,1,2-trichloroethane.
    EXAMPLE 2 Experimental conditions are the same as in Example 1, except that 1.35 kg of 1,2-dichloroethane are added and 1.3 g of trimethylamine are added to the reaction solution instead of ammonia. By neutralizing the hydrogen chloride dissolved in the reaction mixture, an appropriate amount of trimethylammonium chloride is formed. The molar ratio of ferric chloride (III) to trimethylammonium chloride is 1: 1.12. The hourly yield of 1,2-dichloroethane is about 275 g. The content of FeCl, determined colorimetrically in solution, is 0.13% by weight.
    Analysis of the product A, obtained in the condenser after the end of the reaction, gives the following results, wt%;
    1, 1,1,2-ЕТС
    HC1
    Other
    99.86 0.12 0.015 0.006
    Example 3: Experimental conditions are the same as in Example 2, except that 1.7 g of FeCl and 0.65 g of diamine ethane are added as a catalyst to the reaction solution. Due to the neutralization of the dissolved hydrogen chloride in the reaction mixture, an appropriate amount of diaminoethane hydrochloride is formed. The molar ratio of ferric chloride (III) to diamine ethane chlorohydrate is 1: 0.97. The content of FeClj, determined colorimetrically in solution, is
    about 0.07 May,%. Hourly dichloroethane 270 g.
    Analysis of the product A produced in the condenser gives the following results, wt%:

    99.20 0.77 0.02 0.01
    Example A run conditions are analogous to example 1, only 1.5 kg of 1,2-dichloroethane are introduced, the amount of catalyst is 3.3 g of FeClj and 3.0 g of triethanolamine. Due to the neutralization of hydrogen chloride dissolved in the reaction mixture, an appropriate amount of triethanolamine hydrochloride is formed. The molar ratio of ferric chloride (III) to triethanolamine chlorohydrate is 1: 1.01. The content of FeClj, determined colorimetrically in the reaction solution, is about 0.25 wt.%. Hourly output dichloroethane -265
    Analysis of the product A obtained in the condenser gives the following results, wt%:

    iO, 002 99.63 0.35 0.007 0.01
    PRI me R 5
    , about). In a two-liter round flask equipped with a stirrer and a reflux condenser, 1.5 mg of 1,2-dichloroethane with 12 g of FeClj is heated with stirring. A solution of 2.7 g of hydrogen chloride in 750 g of dichloro-ethane and then a solution of 1.26 g of NHj in 273 g of dichloroethane is added dropwise. The molar ratio of iron (III) chloride to ammonium chloride is 1.0. After cooling, the reaction mixture is filtered and the filter residue is dried. 14.4 g of dry catalyst are obtained.
    6). To obtain 1.2-dichloroethane, a suspension is prepared from 4 g of catalyst prepared according to the method indicated in a, as well as 2 g of FeCl 4
    2.7 kg of 1,2-dichloroethane, and after reducing the volume of the mixture to 2 liters, the mixture is introduced into the loop reactor described in Example 1. The hourly supply of chlorine, ethylene and air to the loop reactor
    is, respectively, 60, 60 and 15 liters, the molar ratio of iron (III) chloride to ammonium chloride is 1: 0.6, the reaction proceeds under conditions similar to example 1. 266 g are obtained.
    1,2-dichloroethane, the experience continues
    6 days. The content of FeCl ,, determined by colorimetric in solution, averages 0.15% by weight. Analysis of product A obtained
    in the condenser, respectively, of the reaction liquid B, after the end of the reaction, gives the following results, wt%:
    25
    SdH., C1
    1,2-EDC
    30. 1,1,2-ЕТС НС1
    Other 0.003 Ex. ymerb. Samples for determining corrosion are placed in a reactor for the technical preparation of 1,2-dichloroethane; samples are subjected to tests according to the proposed method. After 20 days, the samples are removed from the reactor and the losses due to corrosion are determined. When applying the catalyst according to the proposed method and keeping the reaction temperature of 100-110 ° C, the average corrosion rate for unalloyed steel is less than 0.05 mm per year. With the known method, when applying Fed, the average corrosion rate for unalloyed steel is 0.43 mm per year,
    Example 7, Analogous to Example 1, 1, but the molar ratio of iron (III) chloride to ammonium chloride is 1: 1.5 in the resulting 1, 2-dichloroethane cheese. 0.1 wt.% Is determined. % 1,1,2-trichloroethane and 0.001 wt.% Lauric hydrogen.
    权利要求:
    Claims (1)
    [1]
    A catalyst for the continuous production of 1,2-dichloroethane by the reaction of ethylene with chlorine containing anhydrous iron (III) chloride and a nitrogen-containing compound, characterized in that, in order to reduce its corrosion and increase selectivity, it contains a compound selected from the group as a nitrogen-containing compound including ammonium chloride, trimethylammonium chloride, diaminoethane hydrochloride, triethanolamine hydrochloride, with a molar ratio of iron (III) hppvord: nitrogen-containing compound 1: (0.6-1.5).
    '3 ω s>
    cm
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    同族专利:
    公开号 | 公开日
    NO158621C|1988-10-12|
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    ES517410A0|1983-08-16|
    MX162900B|1991-07-08|
    BR8207099A|1983-10-11|
    CA1189057A|1985-06-18|
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    AU9161582A|1983-06-16|
    ZA828976B|1983-10-26|
    ES8307529A1|1983-08-16|
    CS235975B2|1985-05-15|
    DE3148450A1|1983-06-16|
    JPS58104636A|1983-06-22|
    IN156063B|1985-05-04|
    DD208604A5|1984-04-04|
    NO824108L|1983-06-09|
    EP0082342A3|1985-09-18|
    NO158621B|1988-07-04|
    EP0082342A2|1983-06-29|
    AU553255B2|1986-07-10|
    HU193155B|1987-08-28|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    WO1997033849A1|1996-03-13|1997-09-18|Caprolactam Joint-Stock Company|Method of obtaining 1,2-dichloroethane|US2486379A|1946-07-22|1949-11-01|Dow Chemical Co|Manufacture of nuclear halogenated alkenyl-benzene compounds|
    US3723543A|1970-12-21|1973-03-27|Olin Corp|Process for preparing 2,4,4,4-tetrachlorobutanol|
    US4058574A|1972-07-11|1977-11-15|Rhone-Progil|Process for the oxychlorination of hydrocarbons with ammonium chloride|
    GB1422303A|1973-06-11|1976-01-28|Stauffer Chemical Co|Production of ethylene dichloride|
    DE2540291C3|1975-09-10|1984-02-23|Hoechst Ag, 6230 Frankfurt|Process for the continuous production of 1,2-dichloroethane and a catalyst container as part of a device for carrying out the process mentioned|
    AU529847B2|1979-01-10|1983-06-23|Akzo N.V.|Combined chlorinated hydrocarbon-sodium bicarbonate productio|
    US4282165A|1980-03-24|1981-08-04|Argus Chemical Corporation|Preparation of trimethyltin chloride from dimethyltin dichloride|DE3247988A1|1982-12-24|1984-06-28|Hoechst Ag, 6230 Frankfurt|METHOD FOR PRODUCING 1,2-DICHLORETHANE|
    DE3347153A1|1983-12-27|1985-07-04|Hoechst Ag, 6230 Frankfurt|METHOD FOR PRODUCING 1,2-DICHLORETHANE|
    DE3519161A1|1985-05-29|1986-12-04|Hoechst Ag, 6230 Frankfurt|METHOD FOR PURIFYING 1,2-DICHLORETHANE|
    DE10050315C2|2000-10-10|2003-08-21|Uhde Gmbh|Process for dissolving salts in 1,2-dichloroethane by means of ultrasound and device for carrying out the process|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19813148450|DE3148450A1|1981-12-08|1981-12-08|CATALYST MIXTURE AND METHOD FOR PRODUCING 1,2-DICHLORETHANE|
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