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Improvements in or relating to the manufacture of chlorinated paraffin waxes

机译:氯化石蜡生产中或与之相关的改进

摘要

Chlorinated paraffin-wax is separated into fractions of differing molecular weight and chlorine content by short path distillation in very high vacuum, e.g. 10-2 to 10-4 mm. of mercury, in apparatus having condensing and evaporating surfaces which are substantially co-extensive and separated by a distance of not more than a few inches. The mono- and di-chlor compounds can in this way be separated from one another and from the higher chlorinated compounds. If the monochlor compound is desired it is preferable to use a wax of low chlorine content, e.g. 12--15 per cent; if a dichlor compound, a wax of, e.g. 20--26 per cent chlorine content. A chlorinated paraffin-wax containing 19,6 per cent chlorine on distillation at 10-4 mm., the cooled glass condensing surface being about 1 inch from the wax, gave a fraction distilling at 85--135 DEG C. which was largely the monochlor derivative. The next fraction up to 150 DEG C. was essentially dichlor-paraffin wax. The residue gave no distillate up to 200 DEG C. and contained 31,9 per cent chlorine. Specifications 303,078, [Class 32], and 417,659 are referred to.ALSO:Chlorinated paraffin-wax is separated into fractions of differing molecular weight and chlorine content by short path distillation in very high vacuum, e.g. 10-2 to 10-4 mm. of mercury, in apparatus having condensing and evaporating surfaces which are substantially co-extensive and separated by a distance of not more than a few inches. The mono- and di-chlor compounds can in this way be separated from one another and from the higher chlorinated compounds. If the monochlor compound is desired it is preferable to use a wax of low chlorine content, e.g. 12--15 per cent; if a dichlor compound, a wax of e.g. 20--26 per cent chlorine content. A chlorinated paraffin wax containing 19,6 per cent chlorine on distillation at 10-4 mm., the cooled glass condensing surface being about 1 in. from the wax, gave a fraction distilling at 85--135 DEG C. which was largely the monochlor derivative. The next fraction up to 150 DEG C. was essentially dichlor-paraffin wax. The residue gave no distillate up to 200 DEG C. and contained 31,9 per cent chlorine. Specifications 303,078, [Class 32], and 417,659 are referred to.
机译:在非常高的真空度下,例如短程蒸馏,通过短程蒸馏将氯化石蜡蜡分离成具有不同分子量和氯含量的馏分。 10 -2至10 -4 mm。在具有冷凝和蒸发表面的装置中,该冷凝和蒸发表面基本上共同延伸并且相隔不超过几英寸的距离。一氯和二氯化合物可以这种方式彼此分离,也可以与高级氯代化合物分离。如果需要一氯化合物,则优选使用低氯含量的蜡,例如氯。 12--15%;如果是二氯化合物,例如蜡。氯含量为20--26%。在10 -4毫米下蒸馏时含有19.6%氯的氯化石蜡,冷却后的玻璃冷凝表面距离蜡约1英寸,在85-135℃下蒸馏出馏分。主要是一氯衍生物。高达150℃的下一个馏分基本上是二氯石蜡。残留物在最高至200℃下没有馏出物,并含有31.9%的氯。参照规格303,078,[Class 32]和417,659。ALSO:通过在非常高的真空度(例如,真空度)下进行短程蒸馏,将氯化石蜡划分为分子量和氯含量不同的馏分。 10 -2至10 -4 mm。在具有冷凝和蒸发表面的装置中,该冷凝和蒸发表面基本上共同延伸并且相隔不超过几英寸的距离。一氯和二氯化合物可以通过这种方式彼此分离,也可以与高级氯代化合物分离。如果需要一氯化合物,则优选使用低氯含量的蜡,例如氯。 12--15%;如果是二氯化合物,则蜡例如氯含量为20--26%。在10 -4毫米下蒸馏时含有19.6%氯的氯化石蜡,冷却后的玻璃冷凝表面距离蜡约1英寸,在85-135℃下馏出馏分。主要是一氯衍生物。高达150℃的下一个馏分基本上是二氯石蜡。残留物在最高至200℃下没有馏出物,并含有31.9%的氯。请参考规格303,078,[Class 32]和417,659。

著录项

  • 公开/公告号GB452662A

    专利类型

  • 公开/公告日1936-08-26

    原文格式PDF

  • 申请/专利号GB19350006169

  • 发明设计人

    申请日1935-02-26

  • 分类号C10G73/38;

  • 国家 GB

  • 入库时间 2022-08-24 06:04:06

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