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integrated process for purification of waste water of refinery, principally containing ammonia and hydrogen sulfide, and acid gas containing mainly hydrogen sulfide.

机译:炼油厂废水的综合处理,主要包含氨和硫化氢,酸性气体主要包含硫化氢。

摘要

A process for treating refinery waste water mainly containing hydrogen sulphide and ammonia in addition to acid gases effluent mainly containing hydrogen sulphide, said process comprising the following steps: a) stripping in the stripping tower (100) said waste water (1) at a pressure ranging from 8 to 20 bar g in order to produce a gaseous overhead stream (2) essentially containing hydrogen sulphide and water and a liquid bottom stream (4) essentially containing aqueous ammonia; b) stripping in a second stripping tower (110) the stream (4) at 1 to 3 bar g in order to produce a gaseous overhead stream (5-11) of ammonia essentially pure on dry basis and a liquid bottom stream (6) containing less than 1 ppm of hydrogen sulphide and less than 5 ppm of ammonia, said water composition having the requirements to be discharged into the sewer; c) oxidation on oxidizer deficiency to nitrogen and water of the ammonia contained in the stream (11) in the thermal oxidation unit (170), to produce an outlet stream (12) containing 50-150 ppm in volume of ammonia and 80-200 ppm in volume of nitrogen oxides; d) thermal oxidation of the stream (12) in the thermal oxidiser unit (160).
机译:除了主要包含硫化氢的酸性气体流出物之外,还处理主要包含硫化氢和氨的炼厂废水的方法,所述方法包括以下步骤:a)在汽提塔(100)中在一定压力下汽提所述废水(1)。为了产生基本上含有硫化氢和水的气态塔顶料流(2)和基本上含有氨水的液体塔底料流(4),其范围为8-20barg。 b)在第二汽提塔(110)中以1至3barg汽提料流(4),以产生基本上干基纯净的氨气气态塔顶料流(5-11)和液底物流(6)。含有小于1ppm的硫化氢和小于5ppm的氨,所述水组合物具有排放到下水道中的要求; c)在氧化剂缺乏时将热氧化单元(170)中的料流(11)中所含的氨氮和水氧化,以产生含有50-150ppm的氨和80-200ppm的氨的出口料流(12)。氮氧化物的体积ppm; d)在热氧化器单元(160)中的物流(12)的热氧化。

著录项

  • 公开/公告号IT1397745B1

    专利类型

  • 公开/公告日2013-01-24

    原文格式PDF

  • 申请/专利权人 SIIRTEC-NIGI S.P.A.;

    申请/专利号IT2010MI00080

  • 发明设计人 BESTETTI ADALBERTO;

    申请日2010-01-22

  • 分类号C02F1/20;

  • 国家 IT

  • 入库时间 2022-08-21 16:39:22

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