CN101318065B - 含氯废液、废气无公害处理方法及其专用装置 - Google Patents
含氯废液、废气无公害处理方法及其专用装置 Download PDFInfo
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- CN101318065B CN101318065B CN2008100943734A CN200810094373A CN101318065B CN 101318065 B CN101318065 B CN 101318065B CN 2008100943734 A CN2008100943734 A CN 2008100943734A CN 200810094373 A CN200810094373 A CN 200810094373A CN 101318065 B CN101318065 B CN 101318065B
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- Prior art keywords
- gas
- flue gas
- waste
- outlet
- hydrochloric acid
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- 239000002699 waste material Substances 0.000 title claims abstract description 34
- 239000002912 waste gas Substances 0.000 title claims abstract description 28
- 238000003672 processing method Methods 0.000 title claims description 13
- 239000000460 chlorine Substances 0.000 title abstract description 11
- 229910052801 chlorine Inorganic materials 0.000 title abstract description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound 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[Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 title abstract description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nMzAwcHgnIGhlaWdodD0nMzAwcHgnIHZpZXdCb3g9JzAgMCAzMDAgMzAwJz4KPCEtLSBFTkQgT0YgSEVBREVSIC0tPgo8cmVjdCBzdHlsZT0nb3BhY2l0eToxLjA7ZmlsbDojRkZGRkZGO3N0cm9rZTpub25lJyB3aWR0aD0nMzAwLjAnIGhlaWdodD0nMzAwLjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PSc5MS4xJyB5PScxNzAuMCcgY2xhc3M9J2F0b20tMCcgc3R5bGU9J2ZvbnQtc2l6ZTo0MHB4O2ZvbnQtc3R5bGU6bm9ybWFsO2ZvbnQtd2VpZ2h0Om5vcm1hbDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6bm9uZTtmb250LWZhbWlseTpzYW5zLXNlcmlmO3RleHQtYW5jaG9yOnN0YXJ0O2ZpbGw6IzVCQjc3MicgPkg8L3RleHQ+Cjx0ZXh0IHg9JzExOC43JyB5PScxNzAuMCcgY2xhc3M9J2F0b20tMCcgc3R5bGU9J2ZvbnQtc2l6ZTo0MHB4O2ZvbnQtc3R5bGU6bm9ybWFsO2ZvbnQtd2VpZ2h0Om5vcm1hbDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6bm9uZTtmb250LWZhbWlseTpzYW5zLXNlcmlmO3RleHQtYW5jaG9yOnN0YXJ0O2ZpbGw6IzVCQjc3MicgPkM8L3RleHQ+Cjx0ZXh0IHg9JzE0Ni4zJyB5PScxNzAuMCcgY2xhc3M9J2F0b20tMCcgc3R5bGU9J2ZvbnQtc2l6ZTo0MHB4O2ZvbnQtc3R5bGU6bm9ybWFsO2ZvbnQtd2VpZ2h0Om5vcm1hbDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6bm9uZTtmb250LWZhbWlseTpzYW5zLXNlcmlmO3RleHQtYW5jaG9yOnN0YXJ0O2ZpbGw6IzVCQjc3MicgPmw8L3RleHQ+Cjwvc3ZnPgo= data:image/svg+xml;base64,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 Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 107
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 89
- 239000003546 flue gas Substances 0.000 claims abstract description 88
- 239000007788 liquid Substances 0.000 claims abstract description 48
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims abstract description 27
- 239000002918 waste heat Substances 0.000 claims abstract description 25
- 239000007789 gas Substances 0.000 claims description 48
- 238000010791 quenching Methods 0.000 claims description 29
- 239000006096 absorbing agent Substances 0.000 claims description 25
- 239000011552 falling film Substances 0.000 claims description 25
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Abstract
Description
Claims (4)
- 一种含氯废液、废气无公害处理方法,其特征在于:它包括以下步骤:(1)焚烧:将废液、废气通入燃烧器和焚烧炉中进行焚烧,焚烧温度为800℃~1400℃;(2)余热吸收:将由步骤(1)产生的含氯烟气通入急冷式余热锅炉使高温烟气温度由800℃~1400℃降至200℃~300℃,降温时间小于0.3秒;(3)干法除尘:将由步骤(2)得到的烟气通入旋风分离器进行干法除尘;(4)急冷:将由步骤(3)得到的烟气通入急冷塔急冷降温至60℃~70℃;(5)湿法除尘:对由步骤(4)得到的烟气通入文丘里管和气液分离器进行湿法除尘;(6)吸收:步骤(5)的烟气通入降膜吸收器与稀盐酸传热传质,使烟气中的HCl气体溶解于稀盐酸中,水蒸汽冷凝为水;(7)洗涤:将由步骤(6)得到的烟气通入填料塔,在填料塔中加入NaOH和Na2SO3水溶液作为洗涤液,把烟气中的残余的HCl和游离态的Cl2气中和掉,然后排放。
- 2.如权利要求1所述的一种含氯废液、废气无公害处理方法,其特征在于:步骤(6)所 述的稀盐酸的质量浓度为5%〜25%。
- 3.如权利要求1所述的一种含氯废液、废气无公害处理方法,其特征在于:步骤(7)所 述的NaOH和Na2SO3水溶液的质量浓度分别为5%〜10%。
- 4. 一种含氯废液、废气无公害处理装置,它包括燃烧器(1),与燃烧器(1)相连通的焚 烧炉(2),其特征在于:焚烧炉(2)连接着急冷式余热锅炉(3),急冷式余热锅炉(3)出口连 接着一级旋风分离器(4),一级旋风分离器(4)连接着二级旋风分离器(5),一级旋风分离 器(4)和二级旋风分离器(5)的下方的出灰口连接着置换仓(6),二级旋风分离器(5)的 出气口和置换仓(6)的出气口同时与急冷塔(7)上部的烟气进口连通,急冷塔(7)下端的 稀盐酸溶液出口经过泵后有一条支路连通着文丘里管(8),同时另一条支路与设在急冷塔 (7)上部的稀盐酸出口连通;急冷塔(7)的烟气出口连接着文丘里管(8)的烟气进口,文 丘里管⑶的出口与气液分离器(9)连接,气液分离器(9)底部的回流口与急冷塔(7)的 酸液回流口相连通,气液分离器(9)的烟气出口连接着降膜吸收器(10)的烟气进口,降膜 吸收器(10)底部的稀盐酸出口经过泵与降膜吸收器(10)顶部的稀盐酸进口连通,降膜吸 收器(10)的烟气出口与填料塔(12)底侧的烟气进口相连通,填料塔(12)底部的洗涤液出 口经循环泵与填料塔(12)肩部的洗涤液进口相连通,填料塔(12)的顶部为烟囱(11)。
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CN102221213B (zh) * | 2011-04-08 | 2012-10-10 | 北京航天动力研究所 | 含有双甘膦、草甘膦的废气、废水焚烧处理装置 |
CN103868077A (zh) * | 2012-12-10 | 2014-06-18 | 北京航天动力研究所 | 含碘有机废液焚烧及尾气净化处理方法及系统 |
CN103743085B (zh) * | 2014-01-02 | 2016-02-24 | 潍坊亿佳节能控制科技有限公司 | 一种蒸煮废汽余热回收系统及其应用 |
CN107812442A (zh) * | 2017-08-25 | 2018-03-20 | 兰州凯特环境技术工程有限公司 | 一种利用瞬间旋风急冷技术去除焚烧烟气中二噁英的装置及其工艺流程 |
CN107559837A (zh) * | 2017-09-29 | 2018-01-09 | 西安山岳环保科技有限公司 | 一种含氯废液、废气焚烧及尾气处理的方法 |
CN109539283A (zh) * | 2018-11-02 | 2019-03-29 | 上海鉴灵节能环保技术有限公司 | 一种制药母液热能降温回收系统及方法 |
CN109737430A (zh) * | 2019-01-03 | 2019-05-10 | 鲁西化工集团股份有限公司硅化工分公司 | 一种危险废物处理系统及方法 |
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