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Improved Process for the Recovery of Bye-products formed during the Dry-distillation or Gasification of Coal.
Improved Process for the Recovery of Bye-products formed during the Dry-distillation or Gasification of Coal.
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机译:煤炭干馏或气化过程中形成的副产品的回收工艺得到改进。
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29,935. Coke Oven Construction Co., and Marr, J. Dec. 23. Drawings to Specification. Ammonia; ammonium sulphate.-In order to avoid the production of effluent liquors during the treatment of distillation gases, the liquor obtained by cooling the gases to effect a complete separation of the tar, is evaporated to dryness after the separation of the tar and the vapours are passed to an ammonium-sulphate saturator. In carrying out the process, the gases are cooled to 15-35‹ C. to separate the whole of the tar and practically all the water, and, after the separation of the benzole if desired and without reheating, the resulting gases are passed into an ammonium-sulphate saturator. The vapours produced by the evaporation of the ammoniacal liquor, as referred to above, are treated in a separate saturator, care being taken that their temperature is maintained so high that condensation of water is avoided. Or these gases may be mixed with a part or the whole of the main gases, and treated in the same saturator.
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机译:29,935。 Coke Oven Construction Co.和Marr,J. 12月23日。氨;硫酸铵。-为了避免在蒸馏气体处理过程中产生废液,通过冷却气体以实现焦油的完全分离而获得的液体在分离焦油和蒸汽后将其蒸发至干。传递到硫酸铵饱和器。在进行该过程中,将气体冷却至15-35℃,以分离出全部焦油和几乎所有的水,并且,如果需要,在苯甲酰分离后并且不进行重新加热,将所得气体通入硫酸铵饱和剂。如上所述,通过氨水蒸发产生的蒸气在单独的饱和器中处理,要注意将其温度保持在很高的温度,以免水冷凝。或者这些气体可以与部分或全部主要气体混合,并在同一饱和器中处理。
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