CN203079786U - Wastewater zero discharging advanced treatment system - Google Patents

Wastewater zero discharging advanced treatment system Download PDF

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CN203079786U
CN203079786U CN201320113858.XU CN201320113858U CN203079786U CN 203079786 U CN203079786 U CN 203079786U CN 201320113858 U CN201320113858 U CN 201320113858U CN 203079786 U CN203079786 U CN 203079786U
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陈颖颖
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Yunnan Wen Yue Technology Co Ltd
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Abstract

本实用新型涉及一种污水处理系统,提供一种结构设计合理、能有效降解水中致色物质的,水中有机物去除率高的,污水可生化性好的、可全部回收于生产,实现对外零排放的废水零排放深度处理系统,包括集水池、反应罐、磁分离器、微电解沉淀塔及回水池,所述集水池的出口连接反应罐的进口,所述反应罐的出口连接磁分离器进口,所述磁分离器的排水孔与微电解沉淀塔的进水口相连,所述微电解沉淀塔的出水口与回水池的进水口相连接,所述回水池内位于进水口的下方设有高密度纤维丝层。

Figure 201320113858

The utility model relates to a sewage treatment system, which provides a sewage treatment system with a reasonable structure design, which can effectively degrade color-causing substances in water, has a high removal rate of organic matter in water, has good biodegradability of sewage, can be fully recycled in production, and realizes zero discharge to the outside world. The wastewater zero-discharge advanced treatment system includes a sump, a reaction tank, a magnetic separator, a micro-electrolytic precipitation tower, and a return pool. The outlet of the sump is connected to the inlet of the reaction tank, and the outlet of the reaction tank is connected to the inlet of the magnetic separator. , the drainage hole of the magnetic separator is connected with the water inlet of the micro-electrolytic precipitation tower, and the water outlet of the micro-electrolytic precipitation tower is connected with the water inlet of the backwater pool, and the water inlet is located below the water inlet in the backwater pool. Density fiber filament layer.

Figure 201320113858

Description

废水零排放深度处理系统Wastewater zero discharge advanced treatment system

技术领域 technical field

    本实用新型涉及一种污水处理系统,尤其是涉及废水零排放深度处理系统。  The utility model relates to a sewage treatment system, in particular to a zero-discharge advanced treatment system for waste water. the

背景技术 Background technique

我国每年排放的污水量很大,经处理后排放的又不多,对环境造成很大破坏,我国各大水系都产生不同程度的污染,水环境严重恶化。长期以来,造纸废水一直是制约纸业快速发展的问题之一,且如何处理造纸废水也是大家关注的问题。所以,加强污水治理,使之不仅达标排放,而且可大量回用,是十分必要的事情。如此一来,这对消除污染,改善水环境,缓解水资源的不足,节约宝贵的水资源,及促进环保产业的发展等都是十分重要的。  The amount of sewage discharged in our country is very large every year, and the amount discharged after treatment is not much, which has caused great damage to the environment. All major water systems in our country have produced varying degrees of pollution, and the water environment has seriously deteriorated. For a long time, papermaking wastewater has been one of the problems restricting the rapid development of the paper industry, and how to deal with papermaking wastewater is also a concern of everyone. Therefore, it is very necessary to strengthen sewage treatment so that it not only discharges up to the standard, but also can be reused in large quantities. In this way, it is very important to eliminate pollution, improve the water environment, alleviate the shortage of water resources, save precious water resources, and promote the development of environmental protection industries. the

水处理就是利用物理、化学和生物的方法对废水进行处理,使废水净化,减少污染,以至达到废水回收、复用,充分利用水资源。现有的污水处理系统, 不能有效降解水中致色物质,水中的有机物去除率低,处理后的废水泡沫现象严重,出水色度深,不能去除高浓度污水的色度,COD去除率低,处理而得的回用水,易恶化发臭,不能长期循环回用,污水的可生化性低,污水中的COD常常超标排放。  Water treatment is to use physical, chemical and biological methods to treat wastewater, purify wastewater, reduce pollution, and achieve wastewater recycling and reuse, making full use of water resources. The existing sewage treatment system cannot effectively degrade the color-causing substances in the water, the removal rate of organic matter in the water is low, the foaming phenomenon of the treated wastewater is serious, the effluent color is deep, the color of high-concentration sewage cannot be removed, the COD removal rate is low, and the treatment The recycled water obtained is easy to deteriorate and smelly, and cannot be recycled for a long time. The biodegradability of the sewage is low, and the COD in the sewage is often discharged beyond the standard. the

实用新型内容 Utility model content

因此,针对上述的问题,本实用新型提供了一种结构设计合理、能有效降解水中致色物质的,水中有机物去除率高的,污水可生化性好的、可全部回收于生产,实现对外零排放的废水零排放深度处理系统。  Therefore, in view of the above problems, the utility model provides a reasonable structure design, which can effectively degrade color-causing substances in water, has a high removal rate of organic matter in water, and has good biodegradability of sewage, which can be fully recycled in production, and realizes zero external pollution. The discharged wastewater is zero-discharge advanced treatment system. the

为达到上述目的,本实用新型是通过以下技术方案实现的:废水零排放深度处理系统,包括集水池、反应罐、磁分离器、微电解沉淀塔及回水池,所述集水池的出口连接反应罐的进口,所述反应罐的出口连接磁分离器进口,所述磁分离器的排水孔与微电解沉淀塔的进水口相连,所述微电解沉淀塔的出水口与回水池的进水口相连接,所述回水池内位于进水口的下方设有高密度纤维丝层。  In order to achieve the above purpose, the utility model is achieved through the following technical solutions: a waste water zero discharge advanced treatment system, including a sump, a reaction tank, a magnetic separator, a micro-electrolytic precipitation tower and a return pool, the outlet of the sump is connected to a reaction The inlet of the tank, the outlet of the reaction tank is connected to the inlet of the magnetic separator, the drain hole of the magnetic separator is connected to the water inlet of the micro-electrolytic precipitation tower, and the water outlet of the micro-electrolytic precipitation tower is connected to the water inlet of the return pool Connected, a high-density fiber filament layer is arranged below the water inlet in the return pool. the

进一步改进的是:所述微电解沉淀塔包括塔体、设于塔体上的塔盖及进污水管,所述塔体上部设有出水口,所述塔体下部设有集污斗,所述集污斗下部设有排泥口,所述塔体内中部设有让固体颗粒快速沉淀的快速沉淀装置,所述塔体内位于快速沉淀装置的上方设有微电解填料过滤层,所述塔体内位于快速沉淀装置的下部设有缓冲槽,所述进污水管的出水端依次穿过塔盖、微电解填料过滤层及快速沉淀装置与塔体内的缓冲槽相连,所述进污水管的进水口连接磁分离器的排水孔。  A further improvement is: the micro-electrolytic precipitation tower includes a tower body, a tower cover arranged on the tower body and a sewage inlet pipe, the upper part of the tower body is provided with a water outlet, and the lower part of the tower body is provided with a sewage bucket, so The lower part of the sewage collection hopper is provided with a mud discharge port, and the middle part of the tower body is provided with a rapid sedimentation device for rapid sedimentation of solid particles. The tower body is located above the rapid sedimentation device. A buffer tank is located at the lower part of the rapid sedimentation device, and the outlet end of the sewage inlet pipe passes through the tower cover, the micro-electrolysis packing filter layer and the rapid sedimentation device in turn to connect with the buffer tank in the tower body, and the water inlet of the sewage inlet pipe Connect the drain hole of the magnetic separator. the

进一步改进的是:所述塔体内位于微电解填料过滤层的上部还设有生物填料层。  A further improvement is: the tower body is also provided with a biological filler layer on the upper part of the micro-electrolysis filler filter layer. the

进一步改进的是:所述微电解填料过滤层包括设于塔体圆周内侧壁上的圆柱筒体、所述圆柱筒体内设有微电解填料,所述圆柱筒体的上部与下部分别设有滤板,所述各滤板上分别均布有通水微孔。  It is further improved that: the filter layer of the micro-electrolytic packing includes a cylindrical body arranged on the inner wall of the tower body, the micro-electrolytic packing is arranged in the cylindrical body, and the upper part and the lower part of the cylindrical body are respectively provided with a filter. plates, and each of the filter plates is evenly distributed with water-through micropores. the

进一步改进的是:所述快速沉淀装置包括设置在塔体内侧的外圆柱筒体及设于外圆柱筒体内侧的、中部设有供进污水管插入穿孔的内圆柱筒体,所述外圆柱筒体与内圆柱筒体之间沿径向方向斜置均布有复数个缓冲沉淀斜板。  A further improvement is that: the rapid sedimentation device includes an outer cylindrical body arranged on the inside of the tower body and an inner cylindrical body arranged on the inner side of the outer cylindrical body, and the middle part is provided with an inner cylindrical body for inserting and perforating the sewage pipe, and the outer cylindrical body Between the cylinder body and the inner cylindrical cylinder body, a plurality of buffer sedimentation sloping plates are arranged obliquely and evenly in the radial direction. the

进一步改进的是:所述反应罐与磁分离器之间设有将反应罐内泥水抽往磁分离器的抽水泵,所述反应罐的底部还设有控制阀门。  A further improvement is that: a water pump for pumping muddy water in the reaction tank to the magnetic separator is provided between the reaction tank and the magnetic separator, and a control valve is provided at the bottom of the reaction tank. the

进一步改进的是:所述磁分离器与微电解沉淀塔之间设有将磁分离器分离出来的污水打入微电解沉淀塔的水泵。  A further improvement is: a water pump is provided between the magnetic separator and the micro-electrolytic precipitation tower to drive the sewage separated by the magnetic separator into the micro-electrolytic precipitation tower. the

通过采用前述技术方案,本实用新型的有益效果是:本实用新型废水零排放深度处理系统处理时,先将生产中的污水通过管路送入集水池,然后将集水池中的污水抽入反应罐,按顺序加入能够完成沉淀泥水中铬、氰化物及重金属的药剂,充分反应后,加入磁粉、絮凝剂,然后静置处理,静置处理后打开反应罐的阀门,将污泥抽入磁分离器进行泥水分离处理,分离处理后将磁分离器内的上清液抽入微电解沉淀塔内进一步生化处理,从而降解废水中致色物质及悬浮物SS和COD,经微电解沉淀塔进一步沉淀及微电解处理后的污水进入回水池循环利用,所述回水池内的高密度纤维丝层可进一步截流水中的悬浮物及生物絮体,提高出水质量;其结构设计合理,处理工艺步骤简单,能有效降解水中致色物质,水中有机物去除率高,污水可生化性好,可有效地对造纸污水进行处理,将对环境的污染降到最低,使其达到污水排放标准,提高了水循环再利用率。  By adopting the above-mentioned technical scheme, the beneficial effect of the utility model is: when the wastewater zero-discharge advanced treatment system of the utility model is processed, the sewage in production is first sent into the sump through the pipeline, and then the sewage in the sump is pumped into the reaction tank, add in order the agents that can complete the sedimentation of chromium, cyanide and heavy metals in the mud water, after full reaction, add magnetic powder, flocculant, and then stand for treatment, after standing for treatment, open the valve of the reaction tank, and pump the sludge into the magnetic The separator performs mud-water separation treatment. After the separation treatment, the supernatant in the magnetic separator is pumped into the micro-electrolysis precipitation tower for further biochemical treatment, thereby degrading the color-causing substances, suspended solids SS and COD in the wastewater, and further precipitating through the micro-electrolysis precipitation tower. And the sewage treated by micro-electrolysis enters the backwater pool for recycling. The high-density fiber silk layer in the backwater pool can further intercept the suspended solids and biological flocs in the water and improve the quality of the effluent; its structure design is reasonable, and the treatment process steps are simple. It can effectively degrade color-causing substances in water, has a high removal rate of organic matter in water, and has good biodegradability of sewage. It can effectively treat papermaking sewage, minimize environmental pollution, make it meet sewage discharge standards, and improve water recycling. Rate. the

附图说明 Description of drawings

图1是本实用新型实施例的流程示意图。  Fig. 1 is a schematic flow chart of the utility model embodiment. the

具体实施方式 Detailed ways

  下面结合附图对本实用新型作进一步说明:  The utility model will be further described below in conjunction with the accompanying drawings:

实施例: Example:

参考图1,本实施例公开一种废水零排放深度处理系统,包括集水池1、反应罐2、磁分离器3、微电解沉淀塔4及回水池5,所述集水池1的出口连接反应罐2的进口,所述反应罐内按顺序加入能够完全沉淀污水中铬、氰化物及重金属的药剂,充分反应后,然后加入磁粉、絮凝剂,然后静置反应,集水池1进口连接于上道工序,其作用是汇集、储存和均衡造纸废水的水质、水量,所述反应罐2的出口连接磁分离器3进口,所述反应罐2与磁分离器3之间设有将反应罐2内泥水抽往磁分离器的抽水泵,所述反应罐2的底部还设有控制阀门21,磁分离器3采用磁分离,污泥与净水只需3分钟就可完全分离,所述磁分离器3的排水孔与微电解沉淀塔4的入口相连,磁分离器3与微电解沉淀塔4之间设有将磁分离器3分离出来的污水打入微电解沉淀塔4的水泵,所述微电解沉淀塔4包括塔体41、设于塔体41上的塔盖42及进污水管43,所述塔体41上部设有出水口,所述塔体41下部设有集污斗44,所述集污斗44下部设有排泥口,所述塔体41内中部设有让固体颗粒快速沉淀的快速沉淀装置45,所述塔体41内位于快速沉淀装置45的上方设有微电解填料过滤层46,所述塔体41内位于快速沉淀装置45下部设有缓冲槽47,所述进污水管43的出水端依次穿过塔盖42、微电解填料过滤层46及快速沉淀装置45与塔体41内的缓冲槽47相连,所述进污水管43的进水口连接磁分离器3的排水孔, 所述快速沉淀装置45包括设置在塔体41内侧的外圆柱筒体451及设于外圆柱筒体451内侧的、中部设有供进污水管43插入穿孔的内圆柱筒体452,所述外圆柱筒体451与内圆柱筒体452之间沿径向方向斜置均布有复数个缓冲沉淀斜板453, 所述微电解沉淀塔4的出水口与回水池5的进水口相连接,所述回水池5内位于进水口的下方设有高密度纤维丝层51。废水经磁分离器3处理后从进污水管进入沉淀塔体内后经缓冲槽缓冲后向四周扩散,然后平稳的向塔顶流动,污水在上升过程中,密度大于水的固体悬浮物如造纸填料、细小纤维、泥纱等无机颗粒不断的下沉并通过快速沉淀装置,加速沉淀,缓冲沉淀装置的每两块缓冲沉淀斜板相当于一个很小的沉淀池,使颗粒沉淀时间大为缩短,利用竖流原理,达到快速沉淀的目的,从缓冲沉淀装置流过的污水从塔体上部的出水口流入回收池5,回水池内的高密度纤维丝层可进一步截流水中的悬浮物及生物絮体,提高出水质量,所述塔体41内位于微电解填料过滤层46的上部还设有生物填料层48。 Referring to Fig. 1, the present embodiment discloses a waste water zero-discharge advanced treatment system, including a sump 1, a reaction tank 2, a magnetic separator 3, a micro-electrolytic precipitation tower 4 and a return pool 5, and the outlet of the sump 1 is connected to a reaction The inlet of the tank 2, the reagents that can completely precipitate chromium, cyanide and heavy metals in the sewage are added in order in the reaction tank, after fully reacting, then add magnetic powder and flocculant, and then stand for reaction, the inlet of the sump 1 is connected to the upper A process, its role is to collect, store and balance the water quality and water volume of papermaking wastewater, the outlet of the reaction tank 2 is connected to the entrance of the magnetic separator 3, and the reaction tank 2 is arranged between the reaction tank 2 and the magnetic separator 3 The inner muddy water is pumped to the water pump of the magnetic separator. The bottom of the reaction tank 2 is also equipped with a control valve 21. The magnetic separator 3 adopts magnetic separation. The sludge and clean water can be completely separated in only 3 minutes. The drain hole of separator 3 links to each other with the inlet of micro electrolytic precipitation tower 4, is provided with the water pump that the sewage separated by magnetic separator 3 is squeezed into micro electrolytic precipitation tower 4 between magnetic separator 3 and micro electrolytic precipitation tower 4, so The micro-electrolytic precipitation tower 4 includes a tower body 41, a tower cover 42 located on the tower body 41 and a sewage inlet pipe 43, the top of the tower body 41 is provided with a water outlet, and the bottom of the tower body 41 is provided with a sewage bucket 44 The bottom of the dirt collecting bucket 44 is provided with a mud outlet, and the middle part of the tower body 41 is provided with a quick sedimentation device 45 for rapid sedimentation of solid particles. An electrolytic filler filter layer 46, the tower body 41 is located at the bottom of the rapid sedimentation device 45 and is provided with a buffer tank 47, and the water outlet end of the sewage inlet pipe 43 passes through the tower cover 42, the micro-electrolytic filler filter layer 46 and the rapid sedimentation device in sequence 45 is connected to the buffer tank 47 in the tower body 41, the water inlet of the sewage inlet pipe 43 is connected to the drain hole of the magnetic separator 3, and the rapid sedimentation device 45 includes an outer cylindrical body 451 arranged on the inside of the tower body 41 and The inner cylindrical body 452 arranged in the middle of the outer cylindrical body 451 for the insertion of the sewage pipe 43 into the perforation, the outer cylindrical body 451 and the inner cylindrical body 452 are arranged obliquely and evenly in the radial direction There are a plurality of buffer sedimentation inclined plates 453, and the water outlet of the micro-electrolytic precipitation tower 4 is connected with the water inlet of the backwater pool 5, and a high-density fiber filament layer 51 is arranged below the water inlet in the backwater pool 5. After the wastewater is treated by the magnetic separator 3, it enters the sedimentation tower from the sewage inlet pipe, and after being buffered by the buffer tank, it diffuses to the surroundings, and then flows smoothly to the top of the tower. During the rising process of the sewage, solid suspended matter with a density greater than water, such as paper-making fillers Inorganic particles such as fine fibers, mud yarn, etc. sink continuously and pass through the rapid sedimentation device to accelerate the sedimentation. Every two buffer sedimentation inclined plates of the buffer sedimentation device are equivalent to a small sedimentation tank, which greatly shortens the particle sedimentation time. Using the principle of vertical flow to achieve the purpose of rapid sedimentation, the sewage flowing from the buffer sedimentation device flows into the recovery tank 5 from the outlet on the upper part of the tower body, and the high-density fiber filament layer in the return tank can further intercept the suspended solids and biological flocs in the water Body, improve water quality, the top of the micro-electrolysis filler filter layer 46 is also provided with a biological filler layer 48 in the tower body 41.

所述微电解填料过滤层46包括设于塔体41圆周内侧壁上的圆柱筒体、所述圆柱筒体内设有微电解填料,所述圆柱筒体的上部与下部分别设有滤板,所述各滤板上分别均布有通水微孔。本新型废水零排放深度处理系统能利用填充在废水中的微电解材料自身产生1.2V电位差对废水进行电解处理,以达到降解有机污染物的目的。通水后,微电解填料筒内会形成无数的微电池系统,在其作用空间构成一个电场。在处理过程中产生的新生态[H] 、Fe2 + 等能与废水中的许多组分发生氧化还原反应,比如能破坏有色废水中的有色物质的发色基团或助色基团,甚至断链,达到降解脱色的作用;生成的Fe2 + 进一步氧化成Fe3 +,它们的水合物具有较强的吸附、絮凝活性,特别是在加碱调pH 值后生成氢氧化亚铁和氢氧化铁胶体絮凝剂,它们的吸附能力远远高于一般药剂水解得到的氢氧化铁胶体,能大量吸附水中分散的微小颗粒,金属粒子及有机大分子,其工作原理基于电化学、氧化、还原、物理吸附以及絮凝沉淀的共同作用对废水进行处理.具有适用范围广、处理效果好、成本低廉、操作维护方便,不需消耗电力资源等优点。  The micro-electrolysis filler filter layer 46 comprises a cylinder body arranged on the inner wall of the tower body 41, the micro-electrolysis filler is arranged in the cylinder body, and the upper and lower parts of the cylinder body are respectively provided with a filter plate. Each of the filter plates is evenly distributed with water-through micropores. The new wastewater zero-discharge advanced treatment system can use the micro-electrolytic material filled in the wastewater to generate a 1.2V potential difference to electrolyze the wastewater to achieve the purpose of degrading organic pollutants. After passing through the water, countless micro-battery systems will be formed in the micro-electrolysis packing cylinder, forming an electric field in its action space. The new ecology [H] and Fe 2 + produced in the process of treatment can undergo redox reactions with many components in wastewater, such as chromophores or auxochromes that can destroy colored substances in colored wastewater, and even chain breaking to achieve degradation and decolorization; the generated Fe 2 + is further oxidized to Fe 3 + , and their hydrates have strong adsorption and flocculation activities, especially after adding alkali to adjust the pH value, ferrous hydroxide and hydrogen are formed Iron oxide colloidal flocculants, their adsorption capacity is much higher than that of ferric hydroxide colloids obtained by hydrolysis of general medicaments, and can absorb a large number of tiny particles, metal particles and organic macromolecules dispersed in water. Its working principle is based on electrochemistry, oxidation, reduction , physical adsorption and flocculation sedimentation to treat wastewater. It has the advantages of wide application range, good treatment effect, low cost, convenient operation and maintenance, and no need to consume power resources.

以上所记载,仅为利用本创作技术内容的实施例,任何熟悉本项技艺者运用本创作所做的修饰、变化,皆属本创作主张的专利范围,而不限于实施例所揭示者。  The above records are only examples of using the technical content of this creation. Any modifications and changes made by those who are familiar with this technology using this creation belong to the scope of patents claimed by this creation, and are not limited to those disclosed in the examples. the

Claims (7)

1.废水零排放深度处理系统,其特征在于:包括集水池、反应罐、磁分离器、微电解沉淀塔及回水池,所述集水池的出口连接反应罐的进口,所述反应罐的出口连接磁分离器进口,所述磁分离器的排水孔与微电解沉淀塔的进水口相连,所述微电解沉淀塔的出水口与回水池的进水口相连接,所述回水池内位于进水口的下方设有高密度纤维丝层。 1. Wastewater zero-discharge advanced treatment system, characterized in that: it includes a sump, a reaction tank, a magnetic separator, a micro-electrolytic precipitation tower and a return pool, the outlet of the sump is connected to the inlet of the reaction tank, and the outlet of the reaction tank Connect the inlet of the magnetic separator, the drain hole of the magnetic separator is connected with the water inlet of the micro-electrolytic precipitation tower, the water outlet of the micro-electrolytic precipitation tower is connected with the water inlet of the return pool, and the return pool is located at the water inlet There is a layer of high-density fiber filaments underneath. 2.根据权利要求1所述的废水零排放深度处理系统,其特征在于:所述微电解沉淀塔包括塔体、设于塔体上的塔盖及进污水管,所述塔体上部设有出水口,所述塔体下部设有集污斗,所述集污斗下部设有排泥口,所述塔体内中部设有让固体颗粒快速沉淀的快速沉淀装置,所述塔体内位于快速沉淀装置的上方设有微电解填料过滤层,所述塔体内位于快速沉淀装置的下部设有缓冲槽,所述进污水管的出水端依次穿过塔盖、微电解填料过滤层及快速沉淀装置与塔体内的缓冲槽相连,所述进污水管的进水口连接磁分离器的排水孔。 2. The wastewater zero-discharge advanced treatment system according to claim 1, characterized in that: the micro-electrolytic precipitation tower includes a tower body, a tower cover and a sewage inlet pipe arranged on the tower body, and the upper part of the tower body is provided with Water outlet, the lower part of the tower body is provided with a sewage collecting bucket, the lower part of the sewage collecting bucket is provided with a mud discharge port, the middle part of the tower body is provided with a rapid sedimentation device for rapid sedimentation of solid particles, and the rapid sedimentation device is located in the tower body A filter layer of micro-electrolysis packing is provided above the device, and a buffer tank is provided at the lower part of the rapid sedimentation device in the tower body. The buffer tanks in the tower body are connected to each other, and the water inlet of the sewage inlet pipe is connected to the drain hole of the magnetic separator. 3.根据权利要求2所述的废水零排放深度处理系统,其特征在于:所述塔体内位于微电解填料过滤层的上部还设有生物填料层。 3. The zero-discharge advanced treatment system for wastewater according to claim 2, characterized in that: the tower body is also provided with a biological filler layer on the upper part of the micro-electrolytic filler filter layer. 4.根据权利要求2所述的废水零排放深度处理系统,其特征在于:所述微电解填料过滤层包括设于塔体圆周内侧壁上的圆柱筒体、所述圆柱筒体内设有微电解填料,所述圆柱筒体的上部与下部分别设有滤板,所述各滤板上分别均布有通水微孔。 4. The wastewater zero-discharge advanced treatment system according to claim 2, characterized in that: the micro-electrolysis filler filter layer includes a cylindrical cylinder arranged on the inner wall of the tower body, and a micro-electrolysis filter is arranged in the cylindrical cylinder. As for the filler, the upper and lower parts of the cylinder body are respectively provided with filter plates, and each filter plate is evenly distributed with water-through micropores. 5.根据权利要求2所述的废水零排放深度处理系统,其特征在于:所述快速沉淀装置包括设置在塔体内侧的外圆柱筒体及设于外圆柱筒体内侧的、中部设有供进污水管插入穿孔的内圆柱筒体,所述外圆柱筒体与内圆柱筒体之间沿径向方向斜置均布有复数个缓冲沉淀斜板。 5. The wastewater zero-discharge advanced treatment system according to claim 2, characterized in that: the rapid sedimentation device includes an outer cylindrical body arranged on the inner side of the tower body and an outer cylindrical body arranged on the inner side of the outer cylindrical body. The sewage inlet pipe is inserted into the perforated inner cylindrical body, and a plurality of buffering and sedimentation sloping plates are arranged obliquely and evenly in the radial direction between the outer cylindrical body and the inner cylindrical body. 6.根据权利要求1所述的废水零排放深度处理系统,其特征在于:所述反应罐与磁分离器之间设有将反应罐内泥水抽往磁分离器的抽水泵,所述反应罐的底部还设有控制阀门。 6. The waste water zero-discharge advanced treatment system according to claim 1, characterized in that: a pump for pumping muddy water in the reaction tank to the magnetic separator is provided between the reaction tank and the magnetic separator, and the reaction tank There is also a control valve at the bottom. 7.根据权利要求1所述的废水零排放深度处理系统,其特征在于:所述磁分离器与微电解沉淀塔之间设有将磁分离器分离出来的污水打入微电解沉淀塔的水泵。 7. The waste water zero-discharge advanced treatment system according to claim 1, characterized in that: a water pump is provided between the magnetic separator and the micro-electrolytic precipitation tower to drive the sewage separated by the magnetic separator into the micro-electrolytic precipitation tower .
CN201320113858.XU 2013-03-13 2013-03-13 Wastewater zero discharging advanced treatment system Expired - Fee Related CN203079786U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107721093A (en) * 2017-11-24 2018-02-23 吉林省农业科学院 A kind of intensive culture sewage plural serial stage handling process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107721093A (en) * 2017-11-24 2018-02-23 吉林省农业科学院 A kind of intensive culture sewage plural serial stage handling process

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