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Integrated process for treating refinery waste water containing ammonia and hydrogen sulphide and refinery exhaust acid gas containing hydrogen sulphide

机译:处理含氨和硫化氢的炼油厂废水和含硫化氢的炼油厂废气的综合工艺

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油厂废水的方法,所述方法包括以下步骤:a)在汽提塔(100)中在压力范围内进行汽提所述废水(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),从8至20barg。 b)在第二个汽提塔(110)中以1-3 bar g的压力汽提物流(4),以产生基本上以干基计纯净的氨气气态塔顶物流(5 11)和包含所述水组合物具有小于1ppm的硫化氢和小于5ppm的氨,其具有被排放到下水道中的要求; c)由于氧化剂的缺乏而使热氧化单元(170)中的料流(11)中所含的氨对氮和水的氧化,从而产生出口料流(12),其含有50 150 ppm的氨气和80 200 ppm的氨气氮氧化物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IN2012CN07152A

    专利类型

  • 公开/公告日2015-12-11

    原文格式PDF

  • 申请/专利权人

    申请/专利号IN7152/CHENP/2012

  • 发明设计人 BESTETTI ADALBERTO;

    申请日2012-08-16

  • 分类号C02F101/16;B01D53/58;C01C1/20;B01D53/48;C01B17/04;C02F101/10;C02F1/20;C02F103/36;

  • 国家 IN

  • 入库时间 2022-08-21 14:25:47

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