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METHOD AND APPARATUS FOR DESULFURIZING AND DENITRATING EXHAUST GAS IN DRY SYSTEM

机译:干燥系统中排气中的脱硫和反硝化方法及装置

摘要

PURPOSE:To desulfurize and denitrate an exhaust gas effectively using a dry system by a simple apparatus, by a method wherein the exhaust gas is desulfurized in a gas phase and the temp. range of a denitrating catalyst in subsequently denitrating said gas in a gas phase is specified. CONSTITUTION:An exhaust gas 6 containing SOx and NOx enters a gas phase desulfurizing vessel 2 through a dust collector 1 and water and ammonia are introduced into the desulfurizing vessel 2 to desulfurize the exhaust gas at a controlled temp. in a gas phase. The desulfurized gas enters a denitrating vessel 3 along with excessive ammonia and passed through an activated carbon catalyst layer 5 preliminarily impregnated with ammonium sulfite and dried at a temp. of 100-200 deg.C to remove NOx in the exhaust gas and the denitrated gas is discharged from a pipe 9. Washing water of the desulfurizing vessel 2 and the denitrating vessel 3 enters a dyproduct treating installation 4 and oxidized by air supplied from a pipe 16 and calcium carbonate supplied from the pipe 16 to be converted to ammonia and calcium sulfate by double decomposition. This ammonis is recirculated to the desulfurizing vessel 2 by a pipe 11.
机译:目的:通过简单的设备,通过干式系统,通过一种在气相和温度下对废气进行脱硫的方法,有效地对废气进行脱硫和脱硝。确定随后在气相中使所述气体脱硝的脱硝催化剂的范围。组成:含有SOx和NOx的废气6通过集尘器1进入气相脱硫容器2,水和氨被引入脱硫容器2中以在受控温度下对废气进行脱硫。在气相中。脱硫的气体与过量的氨一起进入脱硝容器3,并通过预先浸渍有亚硫酸铵的活性炭催化剂层5,并在一定温度下干燥。脱硫容器2和脱硝容器3的洗涤水进入100-200℃以除去废气中的NOx,并且脱硝气体从管道9排出。脱硫容器2和脱硝容器3的洗涤水进入副产物处理设备4,并被从脱硫设备供给的空气氧化。管道16和从管道16供应的碳酸钙通过两次分解转化为氨和硫酸钙。该氨气通过管道11再循环到脱硫容器2。

著录项

  • 公开/公告号JPS5814933A

    专利类型

  • 公开/公告日1983-01-28

    原文格式PDF

  • 申请/专利权人 ISHII SUKEZOU;

    申请/专利号JP19810112933

  • 发明设计人 TANAKA MINORU;ISHII SUKEZOU;

    申请日1981-07-21

  • 分类号B01D53/60;B01D53/34;B01D53/74;B01D53/86;B01D53/94;

  • 国家 JP

  • 入库时间 2022-08-22 12:04:18

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