CN207645970U - A kind of air source reactor wastewater treatment equipment - Google Patents
A kind of air source reactor wastewater treatment equipment Download PDFInfo
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- CN207645970U CN207645970U CN201721655875.0U CN201721655875U CN207645970U CN 207645970 U CN207645970 U CN 207645970U CN 201721655875 U CN201721655875 U CN 201721655875U CN 207645970 U CN207645970 U CN 207645970U
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 25
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000010865 sewage Substances 0.000 claims abstract description 26
- 239000002351 wastewater Substances 0.000 claims abstract description 17
- 230000001105 regulatory effect Effects 0.000 claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 claims abstract description 12
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 claims abstract description 6
- 238000000265 homogenisation Methods 0.000 claims abstract description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 17
- 229910021536 Zeolite Inorganic materials 0.000 claims description 16
- 239000010457 zeolite Substances 0.000 claims description 16
- 239000002808 molecular sieve Substances 0.000 claims description 13
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 13
- 239000010802 sludge Substances 0.000 claims description 10
- 238000003860 storage Methods 0.000 claims description 8
- 230000018044 dehydration Effects 0.000 claims description 3
- 238000006297 dehydration reaction Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims 10
- 238000005276 aerator Methods 0.000 claims 2
- 239000000706 filtrate Substances 0.000 claims 2
- 230000005611 electricity Effects 0.000 claims 1
- 238000005273 aeration Methods 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 7
- 238000007254 oxidation reaction Methods 0.000 abstract description 4
- 230000003647 oxidation Effects 0.000 abstract description 3
- 230000002195 synergetic effect Effects 0.000 abstract description 3
- 238000005868 electrolysis reaction Methods 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract 1
- 239000000725 suspension Substances 0.000 abstract 1
- 239000000945 filler Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
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- 239000002245 particle Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
本实用新型公开了一种气源反应堆废水处理装置,包括与车间生产废水连接的原水集水均质调节池,原水集水均质调节池上依次连接沸石分子筛、稳压水箱、多介质过滤器、污水泵、电催化反应器,电催化反应器内设有曝气装置,曝气装置外接气源供给装置和量子臭氧供给装置,排气口连接尾气处理装置;在电催化反应器上设有悬浮物处理装置。本实用新型一种气源反应堆废水处理装置的废水首先进入原水集水均质调节池匀质,然后用污水泵打入电催化反应器中进行电催化反应,反应过程中向电催化反应器中通入氧化性气体,通过电解、催化、氧化的协同作用,废水处理效果好。
The utility model discloses a waste water treatment device for a gas source reactor, which comprises a raw water collection homogeneous regulating pool connected with the production waste water in a workshop. Sewage pump, electrocatalytic reactor, an aeration device is installed in the electrocatalytic reactor, the aeration device is externally connected to an air source supply device and a quantum ozone supply device, and the exhaust port is connected to an exhaust gas treatment device; a suspension device is installed on the electrocatalytic reactor material handling device. The waste water of a gas source reactor waste water treatment device of the utility model first enters the raw water collection homogeneous adjustment tank for homogenization, and then pumps it into the electrocatalytic reactor with a sewage pump to carry out the electrocatalytic reaction. During the reaction, it flows into the electrocatalytic reactor Through the oxidizing gas, through the synergistic effect of electrolysis, catalysis and oxidation, the wastewater treatment effect is good.
Description
技术领域technical field
本实用新型涉及废水处理,更具体地说,它涉及一种气源反应堆废水处理装置。The utility model relates to wastewater treatment, more specifically, it relates to a gas source reactor wastewater treatment device.
背景技术Background technique
水是人类和一切生物赖以生存的基本要素,也是保障工农业和维系自然生态健康必不可少的资源。随着人口的增加、工农业生产的发展及水环境污染程度的日趋严重,许多地区的可用水资源相继出现了危机,严重制约了社会、经济的发展。污水回用是解决水资源危机的重要的、不可或缺的措施,也是一条成本低、见效快的有效途径。污水回用不但可以缓解水资源短缺问题,同时还可以减少污染排放,对改善水环境质量也具有重要的意义。近年来,各种新兴有机污染物在回用污水中被不断检出,给污水回用带来了一定的风险。然而传统处理手段对此类污染物质的去除并没有太大效果,如何去除这种物质就成为一个迫切需要解决的问题。Water is the basic element for the survival of human beings and all living things, and it is also an indispensable resource for safeguarding industry and agriculture and maintaining the health of natural ecology. With the increase of population, the development of industrial and agricultural production, and the increasingly serious pollution of water environment, the available water resources in many areas have been in crisis one after another, seriously restricting the development of society and economy. Sewage reuse is an important and indispensable measure to solve the water resource crisis, and it is also an effective way with low cost and quick results. Sewage reuse can not only alleviate the shortage of water resources, but also reduce pollution discharge, which is also of great significance to improving the quality of water environment. In recent years, various emerging organic pollutants have been continuously detected in reused sewage, which has brought certain risks to the reuse of sewage. However, traditional treatment methods do not have much effect on the removal of such pollutants, and how to remove such substances has become an urgent problem to be solved.
由此可见,随着废水复杂程度越来越复杂,在废水治理中仅仅依赖传统的工艺技术方法已远远解决不了有机物降解和水污染问题。因此,以科学发展思维,不断改进和创新技术方法,实现废水治理资源化循环利用,清洁生产、节能减排是未来生态环境至上目标。It can be seen that as the complexity of wastewater becomes more and more complex, only relying on traditional technological methods in wastewater treatment is far from being able to solve the problems of organic matter degradation and water pollution. Therefore, with scientific development thinking, continuous improvement and innovation of technical methods, the realization of waste water treatment and resource recycling, clean production, energy saving and emission reduction are the supreme goals of the future ecological environment.
实用新型内容Utility model content
针对现有技术存在的不足,本实用新型的目的在于提供一种气源反应堆废水处理装置,废水净化效果好,安全环保。In view of the deficiencies in the prior art, the purpose of the utility model is to provide a waste water treatment device for gas source reactors, which has good waste water purification effect and is safe and environment-friendly.
本实用新型的上述技术目的是通过以下技术方案得以实现的:一种气源反应堆废水处理装置,包括与车间生产废水连接的原水集水均质调节池,依次与原水集水均质调节池串联设置的沸石分子筛、稳压水箱、多介质过滤器,经过多介质过滤器处理过的废水通过污水泵压入电催化反应器,电催化反应器内设有曝气装置,曝气装置外接气源供给装置和量子臭氧供给装置,在电催化反应器上部的排气口与尾气处理装置连接;在电催化反应器一侧设有悬浮物处理装置。The above-mentioned technical purpose of the utility model is achieved through the following technical solutions: a gas source reactor wastewater treatment device, including a raw water collection homogeneous regulating pool connected with the workshop production wastewater, which is connected in series with the raw water collecting homogeneous regulating pool in turn Equipped with zeolite molecular sieve, pressure-stabilizing water tank, and multi-media filter, the wastewater treated by the multi-media filter is pressed into the electrocatalytic reactor through the sewage pump. The electrocatalytic reactor is equipped with an aeration device, and the aeration device is externally connected to an air source The supply device and the quantum ozone supply device are connected to the tail gas treatment device at the exhaust port on the upper part of the electrocatalytic reactor; a suspended matter treatment device is provided on one side of the electrocatalytic reactor.
通过采用上述技术方案,处理后的废水首先进入原水集水均质调节池匀质,然后用污水泵打入电催化反应器中进行电催化反应,反应过程中由臭氧储罐向电催化反应器中通入臭氧,处理后的尾气经尾气处理设备处理后排放,净化达标后的废水由分离器排出,通过电解、催化、氧化的协同作用,废水处理效果好。By adopting the above technical scheme, the treated wastewater first enters the raw water collection homogeneous adjustment tank for homogeneity, and then pumps it into the electrocatalytic reactor for electrocatalytic reaction. During the reaction, the ozone storage tank is sent to the electrocatalytic reactor Ozone is introduced in the middle, and the treated tail gas is discharged after being treated by the tail gas treatment equipment, and the waste water after purification reaches the standard is discharged from the separator. Through the synergistic effect of electrolysis, catalysis and oxidation, the waste water treatment effect is good.
本实用新型进一步设置为,所述量子臭氧供给装置包括臭氧储罐,与臭氧储罐连接的臭氧缓冲罐,臭氧缓冲罐连接管路与电催化反应器连接。The utility model is further configured that the quantum ozone supply device includes an ozone storage tank, an ozone buffer tank connected to the ozone storage tank, and an ozone buffer tank connection pipeline connected to the electrocatalytic reactor.
通过采用上述技术方案,量子臭氧供给装置结构简单,制造方便,且各部件连接稳定,氧化效果更好。By adopting the above technical solution, the quantum ozone supply device has a simple structure, is convenient to manufacture, and the connection of each component is stable, and the oxidation effect is better.
本实用新型进一步设置为,所述电催化反应器与臭氧缓冲罐的连接管路上设置有臭氧阀门。The utility model is further provided that an ozone valve is arranged on the connecting pipeline between the electrocatalytic reactor and the ozone buffer tank.
通过采用上述技术方案,可以根据实际需求通过调节臭氧阀门调节臭氧的流速,调节和控制方便。By adopting the above technical scheme, the flow rate of the ozone can be adjusted by adjusting the ozone valve according to the actual demand, and the adjustment and control are convenient.
本实用新型进一步设置为,所述污水泵与电催化反应器的连接管路上设有电子流量计和调节水阀。The utility model is further configured that an electronic flow meter and a regulating water valve are provided on the connecting pipeline between the sewage pump and the electrocatalytic reactor.
通过采用上述技术方案,电子流量计的设置便于随时观测流经的废水,方便,直观;调节水阀的设置可以方便连接管路上废水的流量。By adopting the above technical scheme, the setting of the electronic flowmeter is convenient for observing the passing waste water at any time, which is convenient and intuitive; the setting of the adjusting water valve can facilitate the flow of the waste water on the connection pipeline.
本实用新型进一步设置为,所述电催化反应器的底部设置有气体分布器。The utility model is further provided that, the bottom of the electrocatalytic reactor is provided with a gas distributor.
通过采用上述技术方案,通入电催化反应器气体可以被气体分布器均匀分布,改善反应效果。By adopting the above technical solution, the gas fed into the electrocatalytic reactor can be evenly distributed by the gas distributor, thereby improving the reaction effect.
本实用新型进一步设置为,所述气体分布器通过格栅板支撑。The utility model is further configured that the gas distributor is supported by a grid plate.
通过采用上述技术方案,气体分布器通过格栅板支撑,格栅板一方面也具有均匀布器的作用了,另一方面对气体分布器起支撑作用,结构稳定。By adopting the above technical solution, the gas distributor is supported by the grid plate, and the grid plate also has the function of uniform distributor on the one hand, and supports the gas distributor on the other hand, so the structure is stable.
本实用新型进一步设置为,所述电催化反应器底部设有排污口,排污口连接污泥脱水装置。The utility model is further configured as follows: a sewage outlet is provided at the bottom of the electrocatalytic reactor, and the sewage outlet is connected to a sludge dewatering device.
通过采用上述技术方案,排污口连接污泥脱水装置,污泥进行脱水处理,脱完水的污泥可以作为泥饼回用。By adopting the above technical scheme, the sewage outlet is connected to a sludge dewatering device, the sludge is dehydrated, and the dehydrated sludge can be reused as a mud cake.
本实用新型进一步设置为,所述沸石分子筛包括初过滤器壳体,设置在初过滤器壳体内的过滤层,设置在过滤层上部的过滤上封头,设置在过滤层下部的过滤下封头。The utility model is further provided that the zeolite molecular sieve comprises a primary filter housing, a filter layer arranged in the primary filter housing, an upper filter head arranged on the upper part of the filter layer, and a lower filter head arranged on the lower part of the filter layer .
通过采用上述技术方案,采用大于填料表面积的复合材料作为底层承托层,过滤掉污水中的一些大颗粒的物质,再通过多介质填料层进一步过滤,除去污水中各中悬浮物、微生物、以及其他微细颗粒,并对污水进行脱色、脱臭、脱氯、去除有机物、去除合成洗涤剂、细菌、病毒及放射性等污染物质。By adopting the above technical scheme, a composite material larger than the surface area of the filler is used as the bottom supporting layer to filter out some large particles in the sewage, and then further filter through the multi-media filler layer to remove suspended solids, microorganisms, and Other fine particles, and decolorize, deodorize, dechlorinate, remove organic matter, remove synthetic detergents, bacteria, viruses and radioactive pollutants.
本实用新型进一步设置为,所述多介质过滤器包括多介质过滤壳体,设置在多介质过滤壳体内的合成介质过滤层,设置在合成介质过滤层上的滤料上封头,设置在合成介质过滤层下部的滤料下封头,多介质过滤壳体的侧壁上分别设有进水口、进气口、出水口和排水口,多介质过滤壳体的顶部设有排气口。The utility model is further configured as follows: the multi-media filter includes a multi-media filter housing, a synthetic medium filter layer arranged in the multi-media filter housing, an upper head of the filter material arranged on the synthetic medium filter layer, and an upper seal head arranged on the synthetic medium filter layer The bottom head of the filter material in the lower part of the media filter layer, the side walls of the multimedia filter housing are respectively provided with water inlet, air inlet, water outlet and drain, and the top of the multimedia filter housing is provided with an exhaust port.
通过采用上述技术方案,进入多介质过滤器中的污水经过合成介质过滤层过滤,过滤掉污水中的悬浮物、微生物、以及其他微细颗粒。By adopting the above-mentioned technical scheme, the sewage entering the multi-media filter is filtered through the synthetic medium filter layer to filter out suspended solids, microorganisms, and other fine particles in the sewage.
本实用新型进一步设置为,所述合成介质过滤层包括设置在底部的过滤底层承托层,设置在过滤底层承托层上的沸石分子筛层,设置在沸石分子筛层上的多介质过滤层。The utility model is further provided that the synthetic medium filter layer includes a filter bottom support layer arranged at the bottom, a zeolite molecular sieve layer arranged on the filter bottom support layer, and a multi-media filter layer arranged on the zeolite molecular sieve layer.
通过采用上述技术方案,采用大于填料表面积介质作为底层承托层,过滤掉污水中的一些大颗粒的物质,再通过多介质填料层进一步过滤,除去污水中各中悬浮物、微生物、以及其他微细颗粒,最后通过合成介质过滤层,对污水进行脱色、脱臭、脱氯、去除有机物、去除合成洗涤剂、细菌、病毒及放射性等污染物质。By adopting the above technical scheme, using a medium larger than the surface area of the filler as the bottom supporting layer to filter out some large particles in the sewage, and then further filter through the multi-media filler layer to remove suspended solids, microorganisms, and other fine particles in the sewage. Particles, and finally pass through the synthetic medium filter layer to decolorize, deodorize, dechlorinate, remove organic matter, remove synthetic detergents, bacteria, viruses and radioactive pollutants.
综上所述,本实用新型一种气源反应堆废水处理装置具有以下有益效果:处理后的废水首先进入原水集水均质调节池匀质,然后用污水泵打入电催化反应器中进行电催化反应,反应过程中由臭氧储罐向电催化反应器中通入臭氧,处理后的尾气经尾气处理设备处理后排放,净化达标后的废水由分离器排出,通过电解、催化、氧化的协同作用对废水进行处理,废水处理效果好。In summary, a gas source reactor wastewater treatment device of the utility model has the following beneficial effects: the treated wastewater first enters the raw water collection homogeneity regulating pool for homogenization, and then is driven into the electrocatalytic reactor by a sewage pump for electrocatalytic treatment. Catalytic reaction. During the reaction process, ozone is introduced into the electrocatalytic reactor from the ozone storage tank, and the treated tail gas is discharged after being treated by the tail gas treatment equipment. The effect is to treat the wastewater, and the wastewater treatment effect is good.
附图说明Description of drawings
图1为本实施例的结构示意图;Fig. 1 is the structural representation of present embodiment;
图2为本实施例电催化反应器的结构示意图;Fig. 2 is the structural representation of the electrocatalytic reactor of the present embodiment;
图3为本实施例电催化反应器的俯视图;Fig. 3 is the top view of the electrocatalytic reactor of the present embodiment;
图4为本实施例电催化反应器内曝气装置与气体分布器的结构示意图;Fig. 4 is a schematic structural view of the aeration device and the gas distributor in the electrocatalytic reactor of the present embodiment;
图5为本实施例中沸石分子筛的结构示意图;Fig. 5 is the structural representation of zeolite molecular sieve in the present embodiment;
图6为本实施例中多介质过滤器的结构示意图。Fig. 6 is a schematic structural diagram of the multimedia filter in this embodiment.
图中:1、原水集水均质调节池;2、稳压水箱;3、污水泵;4、电催化反应器;51、沸石分子筛;510、初过滤器壳体;511、过滤层;512、过滤上封头;513、过滤下封头;514、过滤底层承托层;515、多介质填料层;52、多介质过滤器;520、多介质过滤壳体;521、合成介质过滤层;522、滤料上封头;523、滤料下封头;524、过滤底层承托层;525、沸石分子筛层;526、多介质过滤层;6、曝气装置;7、气源供给装置;8、尾气处理装置;9、悬浮物处理装置;91、离心滚筒;92、驱动电机;93、悬浮物收集槽;94、悬浮物排放管;95、卸污阀;11、电子流量计;12、调节水阀;13、量子臭氧供给装置;131、臭氧储罐;132、臭氧缓冲罐;133、臭氧阀门;14、气体分布器;15、格栅板;16、污泥脱水装置。In the figure: 1. Raw water collection homogeneous regulating tank; 2. Stabilized water tank; 3. Sewage pump; 4. Electrocatalytic reactor; 51. Zeolite molecular sieve; , filter upper head; 513, filter lower head; 514, filter bottom supporting layer; 515, multi-media packing layer; 52, multi-media filter; 520, multi-media filter shell; 521, synthetic media filter layer; 522. Upper head of filter material; 523. Lower head of filter material; 524. Bottom support layer of filter; 525. Zeolite molecular sieve layer; 526. Multimedia filter layer; 6. Aeration device; 7. Air source supply device; 8. Exhaust gas treatment device; 9. Suspended matter treatment device; 91. Centrifugal drum; 92. Drive motor; 93. Suspended matter collection tank; 94. Suspended matter discharge pipe; 95. Discharge valve; 11. Electronic flow meter; 12 13. Quantum ozone supply device; 131. Ozone storage tank; 132. Ozone buffer tank; 133. Ozone valve; 14. Gas distributor; 15. Grid plate; 16. Sludge dehydration device.
具体实施方式Detailed ways
下面结合附图和实施例,对本实用新型一种气源反应堆废水处理装置进行详细描述。A gas source reactor waste water treatment device of the present utility model will be described in detail below in conjunction with the accompanying drawings and embodiments.
一种气源反应堆废水处理装置,如图1所示,车间生产废水通过连接管路连接至原水集水均质调节池1,原水集水均质调节池1依次与沸石分子筛51、稳压水箱2和多介质过滤器52连接,经过多介质过滤器52处理过的废水通过污水泵3压入电催化反应器4,电催化反应器4内设有曝气装置6,曝气装置6外接气源供给装置7和尾气处理装置8,在电催化反应器4上部的排气口与尾气处理装置8连接;在电催化反应器4底部的排污口与污泥脱水装置16连接。A gas source reactor waste water treatment device, as shown in Figure 1, the production waste water in the workshop is connected to the raw water collection homogeneous regulating tank 1 through the connecting pipeline, and the raw water collecting homogeneous regulating tank 1 is sequentially connected with the zeolite molecular sieve 51 and the pressurized water tank 2 is connected with the multimedia filter 52, and the wastewater treated by the multimedia filter 52 is pressed into the electrocatalytic reactor 4 through the sewage pump 3, and the electrocatalytic reactor 4 is provided with an aeration device 6, and the aeration device 6 is externally connected to the air The source supply device 7 and the tail gas treatment device 8 are connected to the tail gas treatment device 8 at the exhaust port on the upper part of the electrocatalytic reactor 4; the sewage outlet at the bottom of the electrocatalytic reactor 4 is connected to the sludge dehydration device 16.
如图2,在电催化反应器4一侧设有悬浮物处理装置9,悬浮物处理装置9包括水平设置在电催化反应器4两内侧壁之间的离心滚筒91,设置在在外侧用于驱动离心滚筒91工作的驱动电机92,设置在离心滚筒91外侧用于收集悬浮物的悬浮物收集槽93,悬浮物收集槽93底部开有悬浮物排放管94,悬浮物排放管94上设有卸污阀95。As shown in Figure 2, a suspended solids treatment device 9 is provided on one side of the electrocatalytic reactor 4, and the suspended solids treatment device 9 includes a centrifugal drum 91 horizontally arranged between the two inner side walls of the electrocatalytic reactor 4, which is arranged on the outside for The drive motor 92 that drives the centrifugal drum 91 to work is arranged on the outside of the centrifugal drum 91 to collect the suspended matter collection tank 93 for collecting suspended matter. Drain valve 95.
如图3,在电催化反应器4的底部设置有气体分布器14,气体分布器14通过格栅板15支撑。As shown in FIG. 3 , a gas distributor 14 is provided at the bottom of the electrocatalytic reactor 4 , and the gas distributor 14 is supported by a grid plate 15 .
如图4,曝气装置6与气体分布器14连通设置,曝气装置6与气体分布器14配合均匀布器,气体分布器14上设有若干开口朝上的喷嘴。As shown in Fig. 4, the aeration device 6 is arranged in communication with the gas distributor 14, and the aeration device 6 and the gas distributor 14 cooperate with a uniform distributor, and the gas distributor 14 is provided with several nozzles with openings facing upwards.
如图5,沸石分子筛51包括初过滤器壳体510,设置在初过滤器壳体510内的过滤层511,设置在过滤层511上部的过滤上封头512,设置在过滤层511下部的过滤下封头513,过滤层511包括由大于填料表面积介质构成的过滤底层承托层514,以及设置在过滤底层承托层514上的多介质填料层515,鹅卵石从下至上颗粒由大至小排布。As shown in Figure 5, the zeolite molecular sieve 51 includes a primary filter housing 510, a filter layer 511 arranged in the primary filter housing 510, a filter upper head 512 arranged on the filter layer 511 top, and a filter layer arranged at the filter layer 511 bottom. The lower head 513, the filter layer 511 includes a filter bottom support layer 514 made of a medium larger than the surface area of the filler, and a multimedia packing layer 515 arranged on the filter bottom support layer 514, and the pebbles are arranged from large to small from bottom to top. cloth.
如图6,多介质过滤器52,包括多介质过滤壳体520,设置在多介质过滤壳体520内的合成介质过滤层521,设置在合成介质过滤层521上的滤料上封头522,设置在合成介质过滤层521下部的滤料下封头523,合成介质过滤层521包括设置在底部的过滤底层承托层524,设置在过滤底层承托层524上的沸石分子筛层525,设置在沸石分子筛层525上的多介质过滤层526,多介质过滤层526采用果壳活性炭填装而成,过滤底层承托层524为沸石,沸石从下至上颗粒由大至小排布。As shown in Figure 6, the multimedia filter 52 includes a multimedia filter housing 520, a synthetic medium filter layer 521 arranged in the multimedia filter housing 520, an upper end cap 522 on the filter material arranged on the synthetic medium filter layer 521, The filter material lower head 523 arranged at the bottom of the synthetic medium filter layer 521, the synthetic medium filter layer 521 includes a filter bottom supporting layer 524 arranged at the bottom, and a zeolite molecular sieve layer 525 arranged on the filter bottom supporting layer 524 is arranged on The multimedia filter layer 526 on the zeolite molecular sieve layer 525 is filled with fruit shell activated carbon, and the filter bottom support layer 524 is zeolite, and the zeolite particles are arranged from large to small from bottom to top.
工作流程:如图1所示,废水首先进入原水集水均质调节池1,经过原水集水均质调节池1匀质后,打开调节水阀12,用污水泵3打入电催化反应器4中进行电催化反应,污水泵3上设有电子流量计11方便流量观测,反应过程中由量子臭氧供给装置13中的臭氧储罐131经臭氧缓冲罐132并通过臭氧阀门133的调节向带有气体分布器14的电催化反应器4中通入臭氧,并与电催化反应器4内反应堆进行协同催化氧化反应,反应过程中产生的尾气排入尾气处理装置8,经处理后排放,反应过程产生的污泥通过污泥脱水装置16处理,脱完水的污泥可以作为泥饼回用。Workflow: As shown in Figure 1, the waste water first enters the raw water collection homogeneous regulating tank 1, after being homogenized in the raw water collecting homogeneous regulating tank 1, the regulating water valve 12 is opened, and the sewage pump 3 is pumped into the electrocatalytic reactor 4, the electrocatalytic reaction is carried out, and the sewage pump 3 is provided with an electronic flow meter 11 to facilitate flow observation. During the reaction, the ozone storage tank 131 in the quantum ozone supply device 13 passes through the ozone buffer tank 132 and is adjusted to the belt by the ozone valve 133. Ozone is introduced into the electrocatalytic reactor 4 with a gas distributor 14, and a synergistic catalytic oxidation reaction is carried out with the reactor in the electrocatalytic reactor 4, and the tail gas generated during the reaction is discharged into the tail gas treatment device 8, discharged after treatment, and reacted The sludge generated in the process is treated by the sludge dewatering device 16, and the dehydrated sludge can be reused as a mud cake.
以上所述仅是本实用新型的优选实施方式,本实用新型的保护范围并不仅局限于上述实施例,凡属于本实用新型思路下的技术方案均属于本实用新型的保护范围。应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理前提下的若干改进和润饰,这些改进和润饰也应视为本实用新型的保护范围。The above descriptions are only preferred implementations of the present utility model, and the protection scope of the present utility model is not limited to the above-mentioned embodiments, and all technical solutions under the idea of the present utility model all belong to the protection scope of the present utility model. It should be pointed out that for those skilled in the art, some improvements and modifications without departing from the principle of the utility model should also be regarded as the protection scope of the utility model.
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| CN109370894A (en) * | 2018-11-15 | 2019-02-22 | 湖北华龙西科生物科技有限公司 | A kind of Horizontal type solid fermentation can system and microorganism Intelligent fermentation |
| CN109370895A (en) * | 2018-11-15 | 2019-02-22 | 湖北华龙西科生物科技有限公司 | A kind of liquid fermentation can system and microorganism Intelligent fermentation |
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| CN109370894A (en) * | 2018-11-15 | 2019-02-22 | 湖北华龙西科生物科技有限公司 | A kind of Horizontal type solid fermentation can system and microorganism Intelligent fermentation |
| CN109370895A (en) * | 2018-11-15 | 2019-02-22 | 湖北华龙西科生物科技有限公司 | A kind of liquid fermentation can system and microorganism Intelligent fermentation |
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