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Process for the purification of flue gases from heating and purification plants for carrying out the process

机译:从加热和净化工厂净化烟道气的方法

摘要

PCT No. PCT/DK81/00118 Sec. 371 Date Aug. 23, 1982 Sec. 102(e) Date Aug. 23, 1982 PCT Filed Dec. 22, 1981 PCT Pub. No. WO82/02151 PCT Pub. Date Jul. 8, 1982.By a process of cleaning flue gases, both solid particles and nitrogen oxides and sulphur dioxide are removed from the flue gas prior to the discharging into the atmospheric air. In order to ensure that almost all the content of sulphur dioxide and nitrogen oxides is removed from the flue gas, said flue gas is initially carried through a shower of aqueous liquid and subsequently through a heat exchanger, in which its temperature is lowered to about 20 DEG -30 DEG C., and then through a film of alkaline liquid, and finally through a second shower of aqueous liquid to pass a sulphuric acid neutralizing liquid in a container before the discharging into the atmospheric air. As a result a simultaneous possibility of utilizing the heat of the flue gas is ensured by means of the heat exchanger. A cleaning plant for carrying out the process comprises an apparatus (2), through which the flue gas cleaned of solid particles is carried. When seen in the flow direction, this apparatus comprises a first flue scrubber (8), in which the flue gas is subjected to a shower of liquid, a two-step heat exchanger (9, 10) permitting a reduction of the temperature of the flue gas to 20 DEG -30 DEG C. After the two-step heat exchanger (9, 10), the apparatus (2) comprises a rotating, conical disc (11) providing a film of milk of lime, through which the flue gas is forced to pass during the continuous flow through the apparatus. After this film of milk of lime, the flue gas passes a shower of liquid emitted from a second flue scrubber (14), and upon said scrubber the flue gas is forced to pass a limy liquid in a container (15).
机译:PCT号PCT / DK81 / 00118秒371日期1982年8月23日秒102(e)日期,1982年8月23日,PCT,1981年12月22日,PCT公开。 WO82 / 02151 PCT公开号1982年7月8日,通过清洁烟气的过程,在排放到大气中之前,从烟气中去除了固体颗粒,氮氧化物和二氧化硫。为了确保从烟道气中除去几乎所有的二氧化硫和氮氧化物,首先将所述烟道气通过含水液体喷淋,然后通过热交换器,在该热交换器中将其温度降低至约20℃。 -30℃,然后通过碱性液体膜,最后通过第二次水性液体喷淋,以在容器中通过硫酸中和液,然后排放到大气中。结果,通过热交换器确保了同时利用烟道气的可能性。用于实施该方法的清洁设备包括设备(2),通过该设备携带清洁了固体颗粒的烟道气。当沿流动方向看时,该设备包括第一烟道洗涤器(8),其中烟道气经过液体喷淋,两级热交换器(9、10)允许降低烟道气的温度。烟气达到20℃-30℃。在两步换热器(9、10)之后,设备(2)包括一个旋转的锥形盘(11),该盘提供石灰乳膜,烟气通过该盘在连续流过设备的过程中,压力被迫通过。在该石灰乳膜之后,烟道气经过从第二烟道洗涤器(14)排放的液体喷淋,并且在所述洗涤器上,烟道气被迫通过容器(15)中的石灰质液体。

著录项

  • 公开/公告号FI78625C

    专利类型

  • 公开/公告日1989-09-11

    原文格式PDF

  • 申请/专利权人 ROEDSGAARDJES MATHIAS NORDLIEN;

    申请/专利号FI19820002920

  • 发明设计人 ANDERSSONFINN;

    申请日1982-08-23

  • 分类号B01D53/34;

  • 国家 FI

  • 入库时间 2022-08-22 06:39:29

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