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Improvements relating to the treatment of gas works effluent

机译:煤气厂污水处理方面的改进

摘要

PICT:0636704/III/1 Ammonium chloride and other constituents are recovered from gas works effluent by washing the raw ammoniacal liquor with benzole to remove monohydric phenols, distilling off free ammonia, concentrating the spent liquor by evaporation, removing higher phenols by solvent extraction, crystallizing ammonium chloride from the resulting liquor and separating the phenols from the solvents. As shown, raw liquor from tank a is washed with benzole from c in a tower b. The benzole is recovered in still d and returned to storage at f while the phenols pass to receiver g by way of a finishing still wherein further benzole is recovered and returned to f. The washed liquor from b is concentrated in a plant comprising a heat exchanger h, reflux heat exchanger i, dissociator j in which free CO2 and H2S are separated from the liquor by spraying the latter at 90 DEG C. on to coke, and still k from which steam, introduced at the bottom, leaves with ammonia at the top and passes through exchangers i and h and a condenser to a tank m, from which any benzole that has been carried over is returned to f. A portion of the spent liquor from k is withdrawn, cooled at o and returned to an ammonia washing plant, while the remainder is concentrated in evaporator n, cooled at p and washed at q with butyl acetate from r, the solvent being recovered in still s and returned to storage at u, higher phenols being passed to tank t. The spent liquor from q then passes through heat exchangers 10 and 11 to a solvent recovery still v, the solvent condensed at 12 and separated at 13 being returned to tank u, while water separated at 13 is returned to the outlet from evaporator n. The spent liquor from v is evaporated in a vacuum crystallizer w from which ammonium chloride passed to centrifuge z, mother liquor being collected in z1. Condensates from w and n are pumped either to an ammonia washing plant or through an active carbon filter y to water drains. The mother liquors gradually build up in thiocyanate and thiosulphate and may be drawn off and concentrated.ALSO:In recovering ammonium chloride (see Group III) and other constituents from gas works effluent, the raw ammoniacal liquor is washed with benzole to remove monohydric phenols, the spent liquor is then distilled to remove free ammonia, concentrated by evaporation and higher phenols are then removed by extraction with butyl acetate. The phenols are separated from the solvents.
机译:从天然气厂废水中回收氯化铵和其他成分,方法是用苯甲酚洗涤粗氨水以除去一元酚,蒸馏除去游离氨,通过蒸发浓缩废液,用溶剂除去更高的酚萃取,从所得液体中结晶出氯化铵,并将苯酚与溶剂分离。如图所示,来自罐a的原液在塔b中用来自c的苯甲醚洗涤。在蒸馏器d中回收苯甲并在f返回储存,同时苯酚通过精制蒸馏器到达接收器g,其中进一步的苯甲醚被回收并返回f。来自b的洗涤液在包含热交换器h,回流热交换器i,离解器j的装置中浓缩,其中通过将90℃下的液体喷洒到焦炭上而将游离的CO 2和H 2 S从液体中分离出来,并且仍然k从底部引入的蒸汽从顶部离开,并在顶部离开氨,并通过交换器i和h和冷凝器进入储罐m,然后,已带入的苯甲醚将从储罐m返回至f。从k中抽出一部分废液,在o冷却,然后返回到氨水洗涤厂,同时将剩余的浓缩液在蒸发器n中浓缩,在p冷却,并在q用乙酸丁酯从r洗涤,溶剂仍在回收中。 s并返回至u储存,更高的酚被转移至t罐。然后,来自q的废液通过热交换器10和11到达溶剂回收釜v,在12处冷凝并在13处分离的溶剂返回到罐u,而在13处分离的水从蒸发器n返回到出口。来自v的废液在真空结晶器w中蒸发,氯化铵从真空结晶器w中流到离心机z,母液收集在z1中。来自w和n的冷凝物被泵送到氨洗厂或通过活性炭过滤器y到排水管。母液在硫氰酸盐和硫代硫酸盐中逐渐积累,可能会被抽出并浓缩。ALSO:在从煤气厂废水中回收氯化铵(参见第III组)和其他成分时,将粗氨水用苯甲腈洗涤以除去一元酚,然后蒸馏废液以除去游离氨,通过蒸发浓缩,然后通过用乙酸丁酯萃取除去高级酚。从溶剂中分离出酚。

著录项

  • 公开/公告号GB636704A

    专利类型

  • 公开/公告日1950-05-03

    原文格式PDF

  • 申请/专利权人 WILLIAM MONCRIEFF CARR;THOMAS NICKLIN;

    申请/专利号GB19470033474

  • 发明设计人

    申请日1947-12-18

  • 分类号C07C37/00;

  • 国家 GB

  • 入库时间 2022-08-24 02:05:21

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