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    • 1. 发明授权
    • Process for the recovery of cyanuric chloride
    • 回收氰尿酰氯的方法
    • US4245092A
    • 1981-01-13
    • US78833
    • 1979-09-25
    • Ralf GoedeckeMartin LiebertWolfgang NischkWolfgang PlotzKurt Puschner
    • Ralf GoedeckeMartin LiebertWolfgang NischkWolfgang PlotzKurt Puschner
    • C07D251/28
    • C07D251/28
    • There is provided a process for the recovery of cyanuric chloride in solid or liquid form from the reaction mixture which results from the trimerization of cyanogen chloride wherein to recover the cyanuric chloride the gaseous reaction mixture is introduced into an apparatus combination consisting essentially of a stripping column and a condenser connected at the outlet side, preferably a head condenser, preferably above the stripping column, and in which the sump of the stripping column is held to the boiling temperature of the cyanuric chloride whereupon the cyanuric chloride contained in the gaseous reaction mixture at the outlet of the condenser is cooled in the range of 146.degree. to 190.degree. C. and to recover the liquid cyanuric chloride in liquid form it is removed as such at the lower end of the stripping column and is either directly or, in a given case, after an intermediate storage led to a spray tower and is sprayed whereupon the solid, fine-grained cyanuric chloride is withdrawn at the bottom of the spray.
    • 提供了一种从反应混合物中回收固体或液体形式的氰尿酰氯的方法,其由氯氰化物的三聚反应产生,其中将氰尿酰氯回收到基本上由汽提塔组成的装置组合 和在出口侧连接的冷凝器,优选地是顶部冷凝器,优选在汽提塔上方,并且其中汽提塔的油槽保持在氰尿酰氯的沸点温度,随后气态反应混合物中包含的氰尿酰氯 将冷凝器的出口冷却在146℃至190℃的范围内,并回收液体形式的液体氰尿酰氯,将其在汽提塔的下端被除去,并且直接或在给定的 情况下,经过中间储存导致喷雾塔喷射后,固体细粒度氰尿酰氯被取出 wn在喷雾的底部。
    • 2. 发明授权
    • Process for the recovery of cyanuric chloride
    • 回收氰尿酰氯的方法
    • US4245091A
    • 1981-01-13
    • US78832
    • 1979-09-25
    • Ralf GoedeckeMartin LiebertWolfgang NischkWolfgang PlotzKurt Puschner
    • Ralf GoedeckeMartin LiebertWolfgang NischkWolfgang PlotzKurt Puschner
    • C07D251/28
    • C07D251/28
    • There is provided a process for the recovery of cyanuric chloride in solid or liquid form from the reaction mixture which results from the trimerization of cyanogen chloride wherein to recover the cyanuric chloride in liquid or solid form the gaseous reaction mixture is introduced into an apparatus combination consisting essentially of a stripping column and a condenser connected at the outlet side, preferably a head condenser, preferably above the stripping column, and in which the sump of the stripping column is held to the boiling temperature of the cyanuric chloride whereupon the cyanuric chloride contained in the gaseous reaction mixture depending on the regulation of the temperature at the outlet of the condenser in the range of 146.degree. to 190.degree. C. is partially condensed, after which to recover the liquid cyanuric chloride in liquid form it is removed as such at the lower end of the stripping column while the residual gas leaving the condenser and still containing cyanuric chloride, which amount of cyanuric chloride is controlled by the temperature at the outlet of the condenser, is led to a separating chamber and the residual cyanuric chloride is recovered there by known process.
    • 提供了从反应混合物中回收固体或液体形式的氰尿酰氯的方法,其由氯氰化物的三聚反应产生,其中回收氯化氰液体或固体形式,将气态反应混合物引入到装置组合 基本上是在出口侧连接的汽提塔和冷凝器,优选地是顶部冷凝器,优选在汽提塔上方,并且其中汽提塔的油槽保持在氰尿酰氯的沸腾温度,因此,氰尿酰氯包含在 根据调节冷凝器出口温度在146°至190℃范围内的气态反应混合物被部分冷凝,之后回收液态的氰尿酰氯,将其在 汽提塔的下端,而残留气体离开冷凝器,仍然含有氰尿酸 通过冷凝器出口处的温度控制氰尿酰氯的量,被导入分离室,通过已知的方法将残留的氰尿酰氯回收到那里。
    • 3. 发明授权
    • Process for the recovery of cyanuric chloride
    • 回收氰尿酰氯的方法
    • US4245090A
    • 1981-01-13
    • US78831
    • 1979-09-25
    • Ralf GoedeckeMartin LiebertWolfgang NischkWolfgang PlotzKurt Puschner
    • Ralf GoedeckeMartin LiebertWolfgang NischkWolfgang PlotzKurt Puschner
    • C07D251/28
    • C07D251/28
    • There is provided a process for the recovery of cyanuric chloride in solid or liquid form from the reaction mixture which results from the trimerization of cyanogen chloride wherein to recover the cyanuric chloride at will in liquid or solid form the gaseous reaction mixture is introduced into an apparatus combination consisting essentially of a stripping column and a condenser connected at the outlet side, preferably a head condenser, preferably above the stripping column, and in which the sump of the stripping column is held to the boiling temperature of the cyanuric chloride whereupon the cyanuric chloride contained in the gaseous reaction mixture depending on the regulation of the temperature at the outlet of the condenser in the range of 146.degree. to 190.degree. C. is partially condensed, after which to recover the liquid cyanuric chloride in liquid form it is removed as such at the lower end of the stripping column and is either directly or, in a given case, after an intermediate storage led to a spray tower and is sprayed whereupon the solid, fine-grained cyanuric chloride is withdrawn at the bottom of the spray tower while the residual gas leaving the condenser and still containing cyanuric chloride, which amount of cyanuric chloride is controlled by the temperature at the outlet of the condenser, is led preferably to a separating chamber and the residual cyanuric chloride is recovered there by known process.
    • 提供了从氯氰化合物三聚反应产生的反应混合物中回收固体或液体形式的氰尿酰氯的方法,其中以随液态或固态形式回收氰尿酰氯,将气态反应混合物引入装置 组合物基本上由汽提塔和在出口侧连接的冷凝器组成,优选地为冷凝器,优选在汽提塔上方,并且其中汽提塔的油槽保持在氰尿酰氯的沸点温度下,然后将氰尿酰氯 包含在气态反应混合物中,取决于冷凝器出口温度在146〜190℃范围内的温度,被部分浓缩,之后回收液态的氰尿酰氯,将其如此除去 在汽提塔的下端,并且在一个给定的情况下是直接的或者在中间储存之后 将其喷射到喷雾塔上,然后将固体细粒度氰尿酰氯在喷雾塔的底部排出,而剩余气体离开冷凝器并仍含有氰尿酰氯,该量的氰尿酰氯由温度控制 在冷凝器的出口处优选引入分离室,并且通过已知的方法将残留的氰尿酰氯回收到那里。