• 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:

    公开号:SU818482A3
    申请号:SU782634049
    申请日:1978-07-12
    公开日:1981-03-30
    发明作者:Алико Мишель；Род Рене；Тинель Адриан
    申请人:Продюи Шимик Южин Кюльман (Фирма)；
    IPC主号:
    专利说明:

    one
    This invention relates to an improved method for the source of 2-mercaptobenzazole (2-MBT), used as a vulcanization accelerator and as a starting product in the synthesis of other vulcanization accelerators.
    A known method of purification of 2-MBT, to Topbffl is that hot technical decomposition of 2-MBT is a solution of an inert organic solvent, such as aliphatic or cycloaliphatic, or aromatic hydrocarbon, having a boiling point xewiter of 60-1.0. ° C, preferably o or m-xylene, then extracted with 2-MBT with a dilute aqueous solution of alkali metal hydroxide followed by acidification of the alkaline extract and separation of the precipitated c. precipitate of the desired product flj.
    This method is characterized by the complexity of the process, as well as the presence of a large amount of contaminated sewage. It uses organic solvents in which 2-MBT is dissolved.
    The closest in technical essence and the achieved result to the proposed is the method of cleaning
    ki 2-MBT, which is that the raw 2-MBT is cleaned of impurities. extraction of the latter with an organic solvent, such as benzene, followed by separation of the 2-MBT by filtration and its addition by refining by treating with an alkali metal alkali metal oxide 2j.
    This method is characterized by the complexity of the process. In the first stage, the treatment of 2-MBT with an aromatic solvent allows the separation of only some of the UI products in an essential product — aniline, benzthiazole, phenyl-thiocyanate, 2-aminothiophenol, sulfur and. some others, and a subsequent treatment with an aqueous solution of alkali is required, similar to the RH method of removing u) by-products, such as diphenylthiourea and others. In addition, a disadvantage of the known method is the presence of a large number of highly polluted waste water tanks.
    The circuit of the invention is the control of the process science.
    权利要求:
    Claims (2)
    [1]
    The goal is achieved by purifying 2-MBT, which is ensured by cleaning the impurities with 2-mb caprobenzene sol by treating the raw product with carbon tetrachloride or 1,1,2,2-tetrahlo with ethylene, followed by separating the product from the dissolved in an organic solvent of impurities, the crude product, containing volatile impurities, can be treated with carbon tetrachloride or 1,1, 1,1,2,2-tetrachloroethylene, either directly or after preliminary separation of volatile impurities by distillation under reduced pressure. NII. Distillation of volatile impurities is preferably carried out at a temperature of 50-220 ° C and a pressure of 10-200 mHg. In a preferred embodiment of the process, the crude product is suspended in carbon tetrachloride or 1,1,2,2-tetrachlorethylene while heating to reflux temperature. hvorytel, If a crude product separated from volatile substances (e.g., aniline and benethiazole, which after recovery is recycled) is subjected to purification, the first phase of the separation of volatile substances can be carried out by distillation in a wide range. The temperature range (100 ° C). In order to avoid the danger of thermal decomposition of 2-MBT, it is preferable that this temperature be below 220 ° C, the most preferable range being 100-150 seconds. A thin-film scraper evaporator can be successfully used, allowing solid matter to be recovered (powder). The vacuum to be maintained in the apparatus depends on the temperature chosen, it is usually in the range of 10-200 mmHg. In the second phase the crude purified 2-MBT obtained after distillation is suspended in four carbon chloride or ", 1,2,2 tetrachlorethylene. If the purification is carried out without preliminary separation of volatile impurities, the crude reaction product is directly suspended The product is recovered in carbon tetrachloride or 1,1,2,2 - tetrachlorethylene. The recirculation substances are recovered (this is done in this case by distilling the soluble phase obtained after separation of the purified phase. Converted into insoluble form 2- In all cases, for the sake of economy, it is preferred to limit the concentration of solids in suspension with the solvent to 200-400 g / l. The impurities are easier to remove impurities, the finer the crushed product is crushed. The processing by the proposed method can be carried out in wide The temperature range is 0-77 ° C (boiling point of carbon tetrachloride at a pressure of 760 mm Hg), preferably in the range of lO-SO C, 0-12l C (boiling point of 1,1,2,2-tetrachloroethylene) 760 mm Hg), preferably in the range of 10-80 ° C. The final recovery of the mercaptobenzthiazole is performed by any known filtration and drying method. The solution after filtration is distilled to recover carbon tetrachloride or 1,1,2,2-tetrachlorethylene and completely or partially separate the products. Recycling. Example 1 At 180 ° C, after exiting the 2-MBT synthesis reactor and after removing gaseous hydrogen sulfide, 1000 g of the reaction product between aniline, sulfur and carbon disulfide of the following composition are taken,%: 2-MBT 83.5 Aniline 3,2 Benzthiazole 2 Various side reaction products11,3 This product is loaded into a scraper evaporator, in which the mouth: infuse temperature and a vacuum of 15 mm Hg. Volatile substances are distilled off and 54 g of a pale yellow oil containing 57.3% aniline and 35.2% benzthiazole are obtained in a condensation re-condensate. The solid product, extracted in an evaporator and crushed, is suspended in 2300 ml of carbon tetrachloride at 2 5 9c. After stirring for 1 hour, the suspension is filtered, washed twice with 300 ml of carbon tetrachloride, drained and dried. 836.5 g of a light yellow product are obtained, containing 99% of 2-MBT, with an mp. (not corrected) 177-180 s. The output of the cleaning process of 99.2%. The fraction containing aniline and benzthiazole is recycled to the synthesis reactor without further processing. The carbon tetrachloride solution, containing the reaction by-products, is distilled to recover and feed the solvent for recycling. A non-distilled fraction weighing 109 g remains, it is fed for recycling to the production of 2 MBT. EXAMPLE 2; According to the procedure described in example 1, but starting from 1,1,2,2-tetrachlorethylene, identical results are obtained. Example 3. At the exit from the synthesis-2-MBT reactor, 1000 g of the reaction product between aniline, sulfur and carbon disulfide of the following composition,%, are taken:, 2-MBT83.5 Aniline3.2 Benzthiazole2 Various reaction by-products 11.3 This product is introduced at stirring for 30 minutes, about 200 ml of 1,1,2,2-tetrachlorethylene, the temperature of which is supported by cooling in the range of 20-25. After stirring for 1 h, the suspension is mercaptobenzothiazole filtered, washed 2-3 times with 300 ml of 1.1.2 , 2-tetrachlorethylene, wring out and dried 827 g of light yellow product are obtained a, containing 98.5% of 2-MW with m. pl. (not corrected) 177-180s. The yield of the purification process is 97.5%. The soluble phase obtained after filtration is obtained by distilling 50 g of a mixture of aniline and benzthiazole, which are recycled. Example 4. According to the procedure described in Example 3, but replacing 1,1,2,2-tetrachlorethylene with carbon tetrachloride, identical results are obtained. Example 5. At 20D ° C, 500 g of the reaction product between aniline, sulfur and carbon disulfide of a composition similar to Example 3, which is injected with stirring for 20 minutes in 1200 ml of carbon tetrachloride, is withdrawn at the outlet of the synthesis reactor 2-MBT. cooled at. After 1 h of stirring, cool before and filter. Washed 3 times with 150-200 CC, dehydrated and dried. Obtain 414 g of 2-MBT light yellow color with a purity of 99%, so pl. (unadjusted) 178.5-180 C. Purification yield 98.5%. Example b. Similarly to Example 5, but replacing carbon tetrachloride with 1000 ml of 1,1,2,2-tetrachloro ethylene and using temperature, purify 2-MBT. After cooling to 25 ° C, filtering and washing 3 times with 200 ml of solvent, dehydration and drying, 411.5 g of 2-MBT of light yellow color with a purity of 98.8% are obtained, m.p. (unadjusted) 178-180 s. Exit cleaning 97.4%. The study of the spectroscopic method of the mass of the product purified by the proposed method shows the absence of a significant amount of impurities of mass 226, 228 and 300 corresponding to aminobenzthiazole, diphenylthiourea and (benzthiazolyl-2) - 3-benzthiazolinthion-2, which are removed in a known way by additional alkaline treatment. The advantage of the proposed method is that it allows to simplify the process technology, due to the use of a selective solvent - carbon tetrachloride or 1,1,2,2-tetrachloroethylene. This method allows easy recycling of intermediate products and unreacted is-. travel substances, and also easy to separate by-products. On the other hand, the problem of wastewater treatment is eliminated, since water is not used in the process. 1. Method for purifying 2-mercaptobenzthiazole from impurities by treating the raw product with an organic solvent and then separating the product from the impurities dissolved in the organic solvent, so that, in order to simplify the process technology, as organic solvent using carbon tetrachloride or 1,1,2,2-tetrachloroethylene. . 2. The method according to claim 1, about t l and and and the fact that the processing is subjected to a crude product containing volatile impurities. 3. The method according to claim 1, wherein the volatile impurities are previously separated from the crude prod- uct by distillation under reduced pressure. 4. A method according to claim 3, characterized by Tei) i, that distillation is carried out at a temperature of 50-220 ° C and a pressure of 10-200 mm Hg. 5. Method according to paragraphs. 1-3, which is based on the fact that the crude product is suspended in carbon tetrachloride or 1,1,2,2-tetrachlorethylene while being heated to the boiling point of the solvent. Sources of information taken into account during the examination 1. USSR Patent No. 334702, cl. C b 7 D 277/72, 1969.
    [2]
    2.Patent UK No. 1359274 cl. C 2 C, 1974 (prototype),
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    同族专利:
    公开号 | 公开日
    DK300378A|1979-01-13|
    US4192804A|1980-03-11|
    CS222268B2|1983-06-24|
    EP0000464A1|1979-01-24|
    IE781396L|1979-01-12|
    CA1097656A|1981-03-17|
    FR2397409A1|1979-02-09|
    IT7868641D0|1978-07-12|
    EP0000464B1|1981-08-12|
    DE2860932D1|1981-11-12|
    JPS5811952B2|1983-03-05|
    DD137226A5|1979-08-22|
    FR2397409B1|1980-01-18|
    JPS5419976A|1979-02-15|
    ES471636A1|1979-02-01|
    IE47028B1|1983-11-30|
    DK145821B|1983-03-14|
    DK145821C|1983-08-29|
    IT1108498B|1985-12-09|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3030373A|1959-05-01|1962-04-17|Monsanto Chemicals|Emulsion purification of mercaptobenzothiazole|
    BE791800A|1971-11-29|1973-05-23|Sumitomo Chemical Co|2-MERCAPTOBENZOTHIAZOLE PREPARATION PROCESS|US4041982A|1976-01-09|1977-08-16|Kieley & Mueller, Inc.|Double wall plug control valve|
    FR2450828B1|1979-03-06|1981-03-27|Ugine Kuhlmann|
    FR2565977B1|1984-06-15|1986-08-29|Atochem|MERCAPTOBENZOTHIAZOLE PURIFICATION PROCESS|
    DE3604705A1|1986-02-14|1987-08-27|Bayer Antwerpen Nv|METHOD FOR THE TREATMENT OF 2-MERCAPTOBENZTHIAZOL CONTAINING TARS|
    FR2617479B1|1987-07-03|1989-12-29|Manuf Landaise Produits Ch|MERCAPTOBENZOTHIAZOLE PURIFICATION PROCESS|
    ITMI20010473A1|2001-03-07|2002-09-09|Cooperativa Ct Ricerche Poly T|CHIRAL STATIONARY PHASES BASED ON 4-AMINO-3,5-DINYTROBENZOIC ACID DERIVATIVES|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7721437A|FR2397409B1|1977-07-12|1977-07-12|
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