首页> 外国专利> Process for producing flue gas gypsum in the course of the flue gas desulphurisation of power station boiler firings

Process for producing flue gas gypsum in the course of the flue gas desulphurisation of power station boiler firings

机译:在电站锅炉燃烧烟气脱硫过程中生产烟气石膏的方法

摘要

Process for producing flue gas gypsum in the course of the flue gas desulphurisation of power station boiler firings. The flue gas is treated in a scrubbing tower with a scrub water suspension containing lime or limestone and the sulphur dioxide thus scrubbed out is converted in the bottom of the scrubbing tower, with feeding in of atmospheric oxygen, by oxidation and by crystallisation into calcium sulphate dihydrate crystals. A circulating stream is drawn off from the bottom of the scrubbing tower and fed into the scrubbing tower via atomisation nozzles. A further crystal suspension stream is continuously drawn off from the bottom of the scrubbing tower and split by means of a cyclone separator into an underflow carrying crystal slurry and an overflow containing solid fines, with the underflow being dewatered, flue gas gypsum being drawn off and the resulting clear liquid being recirculated to the scrubbing tower and with the overflow containing solid fines likewise being recirculated to the scrubbing tower. At least 10% by weight of the solids contained in the crystal suspension have a particle diameter of less than 20 mu m and are carried along as solid fines in the overflow of the cyclone separator. A substream is separated from the overflow and replaced by a solids-free liquid. In this procedure, the particle size of the calcium sulphate dihydrate crystals drawn off is set by control of the amount of the substream, with, by means of throttling the amount of the substream, finer calcium sulphate dihydrate crystals and ... Original abstract incomplete. IMAGE
机译:在电站锅炉燃烧烟气脱硫过程中生产烟气石膏的方法。烟气在洗涤塔中用含有石灰或石灰石的洗涤水悬浮液处理,如此洗涤出来的二氧化硫在洗涤塔的底部转化成氧气,通过氧化和结晶为硫酸钙的方式转化为氧气。二水合物晶体。从洗涤塔的底部排出循环流,并通过雾化喷嘴将其送入洗涤塔。从洗涤塔的底部连续地抽出另外的晶体悬浮液流,并通过旋风分离器将其分成载有晶体浆料的底流和含有固体细粉的溢流,该底流被脱水,烟气石膏被抽出并被除去。所得的澄清液体被再循环到洗涤塔,并且含有固体细粉的溢流同样被再循环到洗涤塔。包含在晶体悬浮液中的固体的至少10重量%具有小于20μm的粒径,并且作为固体细粉随旋风分离器的溢流携带。将子流与溢流分开,并用无固体液体代替。在该程序中,通过控制子物流的量来设定排出的二水合硫酸钙晶体的粒径,并通过节流子物流的量来调节更细的二水合硫酸钙晶体和... 。 <图像>

著录项

  • 公开/公告号DE3727801A1

    专利类型

  • 公开/公告日1988-03-24

    原文格式PDF

  • 申请/专利权人 RHEINISCH-WESTFAELISCHES ELEKTRIZITAETSWERK AG;

    申请/专利号DE19873727801

  • 发明设计人 GEBHARDGEORGDR.RER.NAT.;

    申请日1987-08-20

  • 分类号C01F11/46;B01D53/14;B01D9/00;A62D3/00;B01D53/34;C04B11/26;

  • 国家 DE

  • 入库时间 2022-08-22 06:51:48

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