CN105833691A - 一种草甘膦母液废气的光催化反应组合处理系统 - Google Patents
一种草甘膦母液废气的光催化反应组合处理系统 Download PDFInfo
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- CN105833691A CN105833691A CN201610345335.6A CN201610345335A CN105833691A CN 105833691 A CN105833691 A CN 105833691A CN 201610345335 A CN201610345335 A CN 201610345335A CN 105833691 A CN105833691 A CN 105833691A
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CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 22
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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- 150000003568 thioethers Chemical class 0.000 description 9
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- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitrogen oxide Substances 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- 238000005516 engineering process Methods 0.000 description 7
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Abstract
本发明属于有机磷农药工业废气处理技术领域,具体涉及一种草甘膦母液废气的光催化反应组合处理系统。该系统包括依次串联的预处理系统、光催化反应系统和后端水吸收塔,预处理系统包括依次串联的前端水吸收塔、酸吸收塔和碱吸收塔,光催化反应系统包括依次串联的除雾器和光催化反应器。通过本发明所提供的光催化反应组合处理系统处理草甘膦类母液废气,一方面,可以更为有效的处理此类高浓度有机废气,减少恶臭污染物扩散;另一方面,处理后的有机废气达标排放,为企业解决环保难题的同时保证企业生产环境和社会效益。
Description
技术领域
[0001]本发明属于有机磷农药工业废气处理技术领域,具体涉及一种草甘膦母液废气的光催化反应组合处理系统。
背景技术
[0002]大气污染是我国目前最为突出的环境问题之一,工业品的加工过程中会有大量的挥发性有机化合物和无机化合物产生,此类废气若直接排放至大气中将会影响空气质量,长期来看会影响动植物的生长以及人类的健康,甚至在一定条件下会产生诸如光化学烟雾这样的公害事件。草甘膦作为一种生物性除草剂,其生产过程中会产生一定量的母液,母液在处理过程中会排放大量挥发性有机废气,此类废气的特征污染物为甲醛、so2、nox、氨、氯化氢,常含有酸性气体、普通有机物和恶臭气体。其中S02、NOx在和其他废气混合的过程中生成带有强烈刺激性气味的气体,严重影响了大气环境和空气质量。草甘膦的母液中排放的VOCs—般都含有甲醛、三乙胺、氯甲烷、硫氧化物、氮氧化物、硫醇、硫醚类等。
发明内容
[0003]为解决现有技术的不足,本发明提供了一种草甘膦母液废气的光催化反应组合处理系统。该系统针对草甘膦母液处理过程中产生的废气的特征污染物甲醛、SO2、NOx、氨、氯化氢和其它挥发性有机废气的特性,以光催化反应器为主结合吸收法处理此类挥发性有机废气,处理之后废气通过烟囱达标排放。通过本发明所提供的草甘膦母液废气的光催化反应组合处理系统可以有效的解决草甘膦母液处理废气的处理排放问题,降低废气的超标排放对环境造成的影响,为废气处理达标排放起到保障作用。
[0004] —种草甘膦母液废气的光催化反应组合处理系统,包括依次串联的预处理系统、光催化反应系统和后端水吸收塔,所述预处理系统包括依次串联的前端水吸收塔、酸吸收塔和碱吸收塔,所述光催化反应系统包括依次串联的除雾器和光催化反应器。
[0005] 进一步的,所述酸吸收塔包括入气口、出气口和出液口,所述碱吸收塔包括入气口、出气口和出液口,所述前端水吸收塔连通所述酸吸收塔的入气口,所述酸吸收塔的出气口连通所述碱吸收塔的入气口,所述碱吸收塔的出气口连通所述除雾器,所述酸吸收塔的出液口和/或所述碱吸收塔的出液口接入第一污水处理系统。
[0006]更进一步的,所述第一污水处理系统接入污水循环利用系统。
[0007]进一步的,所述前端水吸收塔包括入气口、出气口和出液口,所述后端水吸收塔包括入气口、出气口和出液口,所述前端水吸收塔的出液口和/或所述后端水吸收塔的出液口接入第二污水处理系统。
[0008]更进一步的,所述第二污水处理系统接入污水排放系统。
[0009]进一步的,在所述前端水吸收塔的前端设置有废气收集装置。
[0010]更进一步的,在所述废气收集装置和所述前端水吸收塔之间设置有引风机。
[0011 ]进一步的,在所述后端水吸收塔的后端设置有排放风机。
[0012]更进一步的,在所述排放风机的后端设置有烟囱。
[0013]更进一步的,在所述烟囱的后端设置有排放装置。
[0014]在以上技术方案中:吸收塔可均为圆柱形塔状结构,材质可为PP;烟囱为圆柱形结构,材质可为PP;光催化反应器为不锈钢材质,优选的,为316L不锈钢;其余基础和构筑物可为钢筋混凝土结构。
[0015]通过本发明所提供的光催化反应组合处理系统处理草甘膦类母液废气,一方面,可以更为有效的处理此类高浓度有机废气,减少恶臭污染物扩散;另一方面,处理后的有机废气达标排放,为企业解决环保难题的同时保证企业生产环境和社会效益。
附图说明
[0016]图1是本发明所提供的草甘膦母液废气的光催化反应组合处理系统的系统流程图。
[0017]附图1中,各标号所代表的结构列表如下:
[0018] 1、废气收集装置,2、引风机,3、前端水吸收塔,4、酸吸收塔,5、碱吸收塔,6、除雾器,7、光催化反应器,8、后端水吸收塔,9、排放风机,10、烟囱,11、排放装置,12、第一污水处理系统,13、第二污水处理系统。
具体实施方式
[0019]以下结合附图对本发明的原理和特征进行描述,所举实施例只用于解释本发明,并非用于限定本发明的范围。
[0020]在一个具体实施方式中,如图1所示,一种草甘膦母液废气的光催化反应组合处理系统,包括依次串联的废气收集装置1、引风机2、前端水吸收塔3、酸吸收塔4、碱吸收塔5、除雾器6、光催化反应器7、后端水吸收塔8、排放风机9和烟囱10。烟囱后端还可以设置排放装置11。前端水吸收塔、酸吸收塔和碱吸收塔组成预处理系统;除雾器和光催化反应器组成光催化反应系统。
[0021 ] 其中:酸吸收塔包括入气口、出气口和出液口,碱吸收塔包括入气口、出气口和出液口,前端水吸收塔连通酸吸收塔的入气口,酸吸收塔的出气口连通碱吸收塔的入气口,碱吸收塔的出气口连通除雾器,酸吸收塔的出液口和碱吸收塔的出液口共同接入第一污水处理系统12,第一污水处理系统接入污水循环利用系统;前端水吸收塔包括入气口、出气口和出液口,后端水吸收塔包括入气口、出气口和出液口,前端水吸收塔的出液口和后端水吸收塔的出液口共同接入第二污水处理系统13,第二污水处理系统接入污水排放系统。
[0022]废气收集装置和前端水吸收塔之间设置引风机,各吸收塔至光催化反应器通过管道连接,光催化反应器与烟囱之间通过设置在烟囱前端的排放风机提供空气流速,最后处理后的废气通过烟囱排放。前端水吸收塔、除雾器和后端水吸收塔产生的吸收废水经收集之后由管道排放至厂区的污水处理系统处理,再由污水排放系统排放。酸吸收塔和碱吸收塔产生的废酸碱液运送至污水处理系统,再由污水循环利用系统进行利用。草甘膦母液处理过程中产生的废气经过该光催化反应组合处理系统处理后,废气达到排放标准,经由烟囱统一排放。
[0023] 应用例I
[0024]特征污染物为易挥发的氯化氢、甲醛以及酸性气体氯甲烷和二氧化硫
[0025]草甘膦母液废气的光催化组合工艺系统运行时,母液废气中T-VOCS的量约为1200mg/m3,总进气量约为30000m3/h,PM10浓度为225mg/m3,其中氯化氢气体浓度为160mg/m3,甲醛气体浓度为225mg/m3,氯甲烧气体浓度为286mg/m3,二氧化硫气体浓度为152mg/m3。经过酸吸收、碱吸收和光催化氧化工艺段之后的气体流量约为27000m3/h,PM10浓度为15mg/m3,氯化氢气体浓度为7.lmg/m3,甲醛气体浓度为0.lmg/m3,氯甲烧气体浓度为8.58mg/m3,二氧化硫气体浓度为4.7mg/m3,结果表明:酸吸收、碱吸收结合光催化氧化工艺段对草甘膦母液废气中氯化氢、甲醛、氯甲烷和二氧化硫的转化处理效率超过95 % ;在经过末端的水吸收工艺之后,经过处理的母液废气中母液废气中T-vocs的为0.4mg/m3,总排气量约为30000m3/h,PMlO浓度为0.56mg/m3,其中氯化氢气体浓度为0.8mg/m3,甲醛气体浓度为未检出,氯甲烧气体浓度为0.lmg/m3,二氧化硫气体浓度为0.5mg/m3,经过草甘膦母液废气的光催化组合工艺处理系统处理后的尾气转化效率超过99.5%,所排放的尾气达到环保标准要求。
[0026] 应用例2
[0027]特征污染物为易挥发的恶臭气味的气体三乙胺、硫醚、硫醇以及易挥发气体的混合物
[0028]草甘膦母液废气的光催化组合工艺系统运行时,母液废气中T-vocs的量约为1100mg/m3,总进气量约为50000m3/h,PM10浓度为175mg/m3,其中三乙胺气体浓度为120mg/m3,甲醛气体浓度为205mg/m3,氮氧化物气体浓度为236mg/m3,硫醚、硫醇气体浓度为135mg/m3。经过酸吸收、碱吸收和光催化氧化工艺段之后的气体流量约为48000m3/h,PM10浓度为
11.5mg/m3,三乙胺气体浓度为2.4mg/m3,甲醛气体浓度为未检出,氮氧化物气体浓度为3.6mg/m3,硫醚、硫醇气体浓度为1.5mg/m3,结果表明:酸吸收、碱吸收结合光催化氧化工艺段对草甘膦母液废气中三乙胺、甲醛、氮氧化物和硫醚、硫醇的转化处理效率超过98%;在经过末端的水吸收工艺之后,经过处理的母液废气中母液废气中T-vocs的为0.55mg/m3,总排气量约为50000m3/h,PM10浓度为0.52mg/m3,其中三乙胺气体浓度为未检出,甲醛气体浓度为未检出,氮氧化物气体浓度为0.lmg/m3,硫醚、硫醇类气体浓度为未检出,经过草甘膦母液废气的光催化组合工艺处理系统处理后的尾气转化效率超过99.7%,所排放的尾气达到环保标准要求。
[0029] 应用例3
[0030]特征污染物为草甘膦母液废气的特征污染物包含易挥发的氯甲烷、甲醛和酸性气体硫氧化物和氮氧化物以及恶臭性气体三乙胺、硫醚硫醇
[0031]草甘膦母液废气的光催化组合工艺系统运行时,母液废气中T-vocs的量约为900mg/m3,总进气量约为25000m3/h,PM10浓度为157mg/m3,其中三乙胺气体浓度为95mg/m3,氯甲烧气体浓度为125mg/m3,甲醛气体浓度为245mg/m3,氮氧化物气体浓度为236mg/m3,二氧化硫气体浓度为85mg/m3。经过酸吸收、碱吸收和光催化氧化工艺段之后的气体流量约为25000m3/h,PMlO浓度为8.5mg/m3,三乙胺气体浓度为0.8mg/m3,甲醛气体浓度为未检出,氮氧化物气体浓度为2.lmg/m3,二氧化硫气体浓度为0.75mg/m3,硫醚、硫醇类气体浓度为
0.78mg/m3结果表明:酸吸收、碱吸收结合光催化氧化工艺段对草甘膦母液废气中三乙胺、氯甲烷、甲醛、氮氧化物和二氧化硫气体的转化处理效率超过97.5%;在经过末端的水吸收工艺之后,经过处理的母液废气中母液废气中T-vocs的为0.55mg/m3,总排气量约为25000m3/h,PMlO浓度为0.60mg/m3,其中三乙胺气体浓度为0.lmg/m3,甲醛气体浓度为未检出,氮氧化物气体浓度为0.lmg/m3,二氧化硫气体浓度为未检出,硫醚、硫醇类气体未检出,经过草甘膦母液废气的光催化组合工艺处理系统处理后的尾气转化效率超过99.7%,所排放的尾气达到环保标准要求。
[0032]本发明的优势在于,对草甘膦母液处理过程中产生的废气处理的工艺进行优化,结合水、酸、碱吸收+光催化反应技术提出了吸收+催化氧化的新型工艺思路,利用各种工艺的特性分类处理各种特征污染物,最终经光催化反应器处理后达标排放,经过该系统处理后废气稳定达标排放。
[0033]以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。
Claims (10)
1.一种草甘膦母液废气的光催化反应组合处理系统,其特征在于:包括依次串联的预处理系统、光催化反应系统和后端水吸收塔,所述预处理系统包括依次串联的前端水吸收塔、酸吸收塔和碱吸收塔,所述光催化反应系统包括依次串联的除雾器和光催化反应器。
2.根据权利要求1所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:所述酸吸收塔包括入气口、出气口和出液口,所述碱吸收塔包括入气口、出气口和出液口,所述前端水吸收塔连通所述酸吸收塔的入气口,所述酸吸收塔的出气口连通所述碱吸收塔的入气口,所述碱吸收塔的出气口连通所述除雾器,所述酸吸收塔的出液口和/或所述碱吸收塔的出液口接入第一污水处理系统。
3.根据权利要求2所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:所述第一污水处理系统接入污水循环利用系统。
4.根据权利要求1所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:所述前端水吸收塔包括入气口、出气口和出液口,所述后端水吸收塔包括入气口、出气口和出液口,所述前端水吸收塔的出液口和/或所述后端水吸收塔的出液口接入第二污水处理系统。
5.根据权利要求4所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:所述第二污水处理系统接入污水排放系统。
6.根据权利要求1所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:在所述前端水吸收塔的前端设置有废气收集装置。
7.根据权利要求6所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:在所述废气收集装置和所述前端水吸收塔之间设置有引风机。
8.根据权利要求1所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:在所述后端水吸收塔的后端设置有排放风机。
9.根据权利要求8所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:在所述排放风机的后端设置有烟囱。
10.根据权利要求9所述的草甘膦母液废气的光催化反应组合处理系统,其特征在于:在所述烟囱的后端设置有排放装置。
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