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Process of treating gas condensate

机译:凝析气处理工艺

摘要

The sewage consists of gas condensates from coal-gasifying plants and/or coal chemical plants and contains the anions SO.sub.4.sup.-- , SCN. sup.-, NO.sub.3.sup.-, Cl.sup.- and F.sup.- in a total of at least 2 mval/l and contains organic matter corresponding to a chemical oxygen demand of at least 1000 mg/l. The sewage is passed through a biological purification stage (8), and a succeeding fine purification stage (13, 17, 18). In an anion exchanger (19), strong anions are exchanged with hydrogen carbonate ions. The water leaving the anion exchange stage has an alkalinity of at least 2 mval/l and is passed at least in part through a cation exchanger (26) before the water is recycled to the sewage (line 5).PPThe water which has left the anion exchanger (19) may be used as cooling water in a cooling tower (21) before or after the cation exchanger (26). Organic acids are used for regeneration in the cation exchanger (26) and the regeneration eluate is added to the sewage which is to be treated in the biological purification stage (8).
机译:污水由煤气化厂和/或煤化工厂的气体冷凝物组成,并包含负离子SO4sub.SCN。上,NO.sub.3.sup。,Cl.sup.-和F.sup.-总量至少为2 mval / l,并​​且含有对应于化学需氧量至少为1000 mg的有机物/ l。污水经过生物净化阶段(8)和随后的精细净化阶段(13、17、18)。在阴离子交换器(19)中,强阴离子与碳酸氢根离子交换。离开阴离子交换阶段的水的碱度至少为2 mval / l,并​​且在将水再循环至污水之前(管线5)至少部分通过阳离子交换器(26)。离开阴离子交换体(19)的水可以在阳离子交换体(26)之前或之后用作冷却塔(21)中的冷却水。将有机酸用于阳离子交换器(26)中的再生,并将再生洗脱液添加至将在生物纯化阶段(8)中处理的污水中。

著录项

  • 公开/公告号US4481112A

    专利类型

  • 公开/公告日1984-11-06

    原文格式PDF

  • 申请/专利权人 HANS HITZEL INC.;

    申请/专利号US19830517880

  • 发明设计人 HANS HITZEL;

    申请日1983-07-27

  • 分类号C02F9/00;

  • 国家 US

  • 入库时间 2022-08-22 08:37:03

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