CN210215006U - 臭氧催化氧化处理煤化工废水的装置 - Google Patents
臭氧催化氧化处理煤化工废水的装置 Download PDFInfo
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- CN210215006U CN210215006U CN201920664746.0U CN201920664746U CN210215006U CN 210215006 U CN210215006 U CN 210215006U CN 201920664746 U CN201920664746 U CN 201920664746U CN 210215006 U CN210215006 U CN 210215006U
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- catalytic oxidation
- ozone catalytic
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- coal chemical
- ozone
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- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound 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[O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 98
- 230000003197 catalytic Effects 0.000 title claims abstract description 88
- 230000003647 oxidation Effects 0.000 title claims abstract description 81
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 81
- 239000002351 wastewater Substances 0.000 title claims abstract description 31
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 239000003245 coal Substances 0.000 title claims abstract description 26
- 239000000126 substance Substances 0.000 title description 12
- 239000007788 liquid Substances 0.000 claims abstract description 34
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Abstract
本实用新型公开了一种臭氧催化氧化处理煤化工废水的装置,其包括一级臭氧催化氧化罐和二级臭氧催化氧化罐,一级臭氧催化氧化罐的结构和二级臭氧催化氧化罐的结构相同,一级臭氧催化氧化罐包括罐体,罐体的顶端设有顶部排气口,顶部排气口下方依次设有除沫装置、液体分布装置、填料压紧装置、液体收集再分配装置、填料压紧装置,除沫装置、液体分布装置、填料压紧装置、液体收集再分配装置都位于罐体内,罐体的底端设有底部排水管。本实用新型循环处理煤化工废水,提高臭氧的利用率。
Description
技术领域
本实用新型涉及一种处理废水的装置,特别是涉及一种臭氧催化氧化处理煤化工废水的装置。
背景技术
我国煤化工产业进行污水处理的过程中使用的是传统的净水工艺,通过传统的物化预处理和生化处理的这种方式不能将废水中的毒害物质进行有效的处理,因此,在这种方式处理下得到的废水依然无法达到规定的废水处理标准,这也在一定的程度上阻碍了煤化工产业的持续发展,严重限制了我国煤化工产业的未来发展前景。所以,对煤化工产业排放的水做深度的处理在降低该产业对环境污染的程度上是非常重要的。
目前在实际应用中臭氧催化氧化罐存在一系列的问题:第一,臭氧与水的传质效果差,臭氧利用效率低。传统的臭氧催化氧化罐受制于产生气泡的大小对气水混合效果的影响作用,缺乏高效的气水混合系统和合理的接触面积控制,使得臭氧利用效率较低。第二,臭氧催化氧化装置中催化剂靠重力堆砌也导致了臭氧与液体之间的接触面积不充分。第三,现有的臭氧催化装置会产生二次污染,并且尾气中臭氧浓度较高,仍不能直接外排。
实用新型内容
本实用新型的目的是为了解决现有技术中存在的缺点,而提出一种臭氧催化氧化处理煤化工废水的装置。
本实用新型是通过下述技术方案来解决上述技术问题的:一种臭氧催化氧化处理煤化工废水的装置,其特征在于,其包括一级臭氧催化氧化罐和二级臭氧催化氧化罐,一级臭氧催化氧化罐的结构和二级臭氧催化氧化罐的结构相同,一级臭氧催化氧化罐包括罐体,罐体的顶端设有顶部排气口,顶部排气口下方依次设有除沫装置、液体分布装置、填料压紧装置、液体收集再分配装置、填料压紧装置,除沫装置、液体分布装置、填料压紧装置、液体收集再分配装置都位于罐体内,罐体的底端设有底部排水管,一级臭氧催化氧化罐的底部排水管与二级臭氧催化氧化罐的上部进水管通过一根第一管道连通,一级臭氧催化氧化罐的顶部排气口与二级臭氧催化氧化罐的顶部排气口通过一根第二管道管连通。
优选地,所述罐体的底部设有一个底部液位孔。
优选地,所述第一管道上设有一个水泵。
优选地,所述填料压紧装置内设有臭氧催化剂。
优选地,所述填料压紧装置的下方设有至少一个曝气盘,曝气盘采用分级布置盘式微孔曝气器。
优选地,所述液体分布装置的侧面、液体收集再分配装置的侧面、曝气盘的侧面都设有一个安装孔。
优选地,所述一级臭氧催化氧化罐的高度和二级臭氧催化氧化罐的高度都设为六米。
本实用新型的积极进步效果在于:本实用新型提供一种臭氧催化氧化处理煤化工废水的装置,将煤化工废水进行预处理;再将废水输入一级臭氧催化氧化罐,进行高级氧化处理;将一级臭氧催化氧化罐的出水输入二级臭氧催化氧化罐,充分利用一级臭氧催化氧化罐的臭氧,其中臭氧通过底部的板式微孔曝气器再次提高臭氧在废水中的利用效率。将二级臭氧催化氧化罐的出水再次输入一级臭氧催化氧化罐中,不停地循环,最大程度降解毒害物质,才将二级臭氧催化氧化罐中的废水输入下一个处理系统。
附图说明
图1为本实用新型臭氧催化氧化处理煤化工废水的装置的结构示意图。
图中:顶部排气口1、除沫装置2、上部进水管3、安装孔4、催化剂5、底部排水管6、液体分布装置7、填料压紧装置8、液体收集再分配装置9、曝气管路10、底部液位孔11、罐体12、水泵13
具体实施方式
下面结合附图给出本实用新型较佳实施例,以详细说明本实用新型的技术方案。
如图1所示,本实用新型臭氧催化氧化处理煤化工废水的装置包括一级臭氧催化氧化罐和二级臭氧催化氧化罐,一级臭氧催化氧化罐的结构和二级臭氧催化氧化罐的结构相同,一级臭氧催化氧化罐包括罐体12,罐体12的顶端设有顶部排气口1,顶部排气口1下方依次设有除沫装置2、液体分布装置7、填料压紧装置8、液体收集再分配装置9、填料压紧装置8,除沫装置2、液体分布装置7、填料压紧装置8、液体收集再分配装置9都位于罐体12内,罐体12的底端设有底部排水管6,一级臭氧催化氧化罐的底部排水管6与二级臭氧催化氧化罐的上部进水管3通过一根第一管道连通,一级臭氧催化氧化罐的顶部排气口1与二级臭氧催化氧化罐的顶部排气口1通过一根第二管道管连通。“液体分布装置7、填料压紧装置8、液体收集再分配装置9”都是现有的结构。
罐体12的底部设有一个底部液位孔11,这样及时了解罐体12的液体情况。
第一管道上设有一个水泵13,这样方便控制进出水。
填料压紧装置8内设有臭氧催化剂5,这样具有降解能力强、臭氧消耗低、无二次汚染、使用寿命长等技术特点。
填料压紧装置8的下方设有至少一个曝气盘10,曝气盘采用分级布置盘式微孔曝气器(0.8~1.9mm),避免了气水面积接触不充分,改善了气泡的大小对气水混合效果的影响,可以大幅度的增强臭氧的利用率,较传统只有底部曝气的方式氧利用率提高20%。
液体分布装置7的侧面、液体收集再分配装置9的侧面、曝气盘10的侧面都设有一个安装孔4,这样方便安装各个元件或装置。,
一级臭氧催化氧化罐的高度和二级臭氧催化氧化罐的高度都可以设为六米,一级臭氧催化氧化罐的排气孔与二级臭氧催化氧化罐上端的排气孔相连,这样充分利用臭氧。
本实用新型臭氧催化氧化处理煤化工废水的装置的工作原理如下:将煤化工废水进行预处理,调Ph值;再将废水输入一级臭氧催化氧化罐中,进行高级氧化处理,其中填料为陶粒;将一级臭氧催化氧化罐的出水输入二级臭氧催化氧化罐,调Ph值,进行高级氧化处理,其中填料为陶粒; 将一级臭氧催化氧化罐的排气口打开通入二级臭氧催化氧化罐,进一步利用臭氧,二级臭氧催化氧化罐出水回流至一级臭氧催化氧化罐,进一步氧化降解有机物。循环时间为1h,二级臭氧催化氧化罐的出水排入到下一个处理系统,其中尾气排入到尾气处理装置中。所述废水在一级臭氧催化氧化罐的液位高度设为4-4.5米,其中罐体高度为六米。所述废水在二级臭氧催化氧化罐的液位高度设为4-4.5米,其中罐体高度为六米。所述填料为陶粒。所述盘式微孔曝气器的开孔孔径为0.8~1.9mm。所述一级臭氧催化氧化罐臭氧供气量是二级臭氧催化氧化罐的2倍。所述循环时间为1h。本实用新型采用两级臭氧催化氧化装置,一级臭氧催化氧化罐的出水输入二级臭氧催化氧化罐,再将二级臭氧催化氧化罐的出水再次输入一级臭氧催化氧化罐中,不停地循环,待COD降为原来的80%以上可排入到下一个处理系统,通过臭氧的降解,大大提高了煤化工废水的可生化性 ,为后续生化处理减轻极大的负荷。
本实用新型在一级臭氧催化氧化罐和二级臭氧催化氧化罐之间循环处理煤化工废水,提高臭氧的利用率。臭氧催化氧化装置减少了后续的处理工艺流程,减少占地面积。本实用新型处理效果比传统臭氧催化氧化的方法提高30~40%,对某些难降解有机物亦有很好的去除效果。
以上所述的具体实施例,对本实用新型的解决的技术问题、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上所述仅为本实用新型的具体实施例而已,并不用于限制本实用新型,凡在本实用新型的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。
Claims (7)
1.一种臭氧催化氧化处理煤化工废水的装置,其特征在于,其包括一级臭氧催化氧化罐和二级臭氧催化氧化罐,一级臭氧催化氧化罐的结构和二级臭氧催化氧化罐的结构相同,一级臭氧催化氧化罐包括罐体(12),罐体(12)的顶端设有顶部排气口(1),顶部排气口(1)下方依次设有除沫装置(2)、液体分布装置(7)、填料压紧装置(8)、液体收集再分配装置(9)、填料压紧装置(8),除沫装置(2)、液体分布装置(7)、填料压紧装置(8)、液体收集再分配装置(9)都位于罐体(12)内,罐体(12)的底端设有底部排水管(6),一级臭氧催化氧化罐的底部排水管(6)与二级臭氧催化氧化罐的上部进水管(3)通过一根第一管道连通,一级臭氧催化氧化罐的顶部排气口(1)与二级臭氧催化氧化罐的顶部排气口(1)通过一根第二管道管连通。
2.如权利要求1所述的臭氧催化氧化处理煤化工废水的装置,其特征在于,所述罐体(12)的底部设有一个底部液位孔(11)。
3.如权利要求1所述的臭氧催化氧化处理煤化工废水的装置,其特征在于,所述第一管道上设有一个水泵(13)。
4.如权利要求1所述的臭氧催化氧化处理煤化工废水的装置,其特征在于,所述填料压紧装置(8)内设有臭氧催化剂(5)。
5.如权利要求1所述的臭氧催化氧化处理煤化工废水的装置,其特征在于,所述填料压紧装置(8)的下方设有至少一个曝气盘(10),曝气盘采用分级布置盘式微孔曝气器。
6.如权利要求5所述的臭氧催化氧化处理煤化工废水的装置,其特征在于,所述液体分布装置(7)的侧面、液体收集再分配装置(9)的侧面、曝气盘(10)的侧面都设有一个安装孔(4)。
7.如权利要求1所述的臭氧催化氧化处理煤化工废水的装置,其特征在于,所述一级臭氧催化氧化罐的高度和二级臭氧催化氧化罐的高度都设为六米。
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