CN203079812U - Advanced sewage treatment system with zero discharge - Google Patents
Advanced sewage treatment system with zero discharge Download PDFInfo
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- CN203079812U CN203079812U CN201320113857.5U CN201320113857U CN203079812U CN 203079812 U CN203079812 U CN 203079812U CN 201320113857 U CN201320113857 U CN 201320113857U CN 203079812 U CN203079812 U CN 203079812U
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- 239000010865 sewage Substances 0.000 title claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000003756 stirring Methods 0.000 claims abstract description 46
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 32
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 239000006148 magnetic separator Substances 0.000 claims abstract description 27
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000012856 packing Methods 0.000 claims abstract description 26
- 239000000945 filler Substances 0.000 claims abstract description 23
- 230000003647 oxidation Effects 0.000 claims abstract description 21
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 21
- 239000000835 fiber Substances 0.000 claims abstract description 5
- 210000003437 trachea Anatomy 0.000 claims description 11
- 239000010802 sludge Substances 0.000 claims description 5
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical group [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 8
- 239000005416 organic matter Substances 0.000 abstract description 5
- 238000013461 design Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 208000028659 discharge Diseases 0.000 abstract 2
- 238000007873 sieving Methods 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 14
- 230000006872 improvement Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
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- 229960004887 ferric hydroxide Drugs 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
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- 238000005187 foaming Methods 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
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- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- IEECXTSVVFWGSE-UHFFFAOYSA-M iron(3+);oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Fe+3] IEECXTSVVFWGSE-UHFFFAOYSA-M 0.000 description 1
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 1
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Water Treatment By Electricity Or Magnetism (AREA)
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、去除水中有机物的,污水可生化性好的,可全部回收于生产,实现对外零排放的污水零排放深度处理系统,包括集水池、过滤滚筛机、搅拌反应塔、磁分离器、微电解填料筒、生物接触氧化池、活性炭过滤器及回水池,集水池的出口连接过滤滚筛机的进口,过滤滚筛机的出口连接搅拌反应塔的进口,搅拌反应塔的出口连接磁分离器进口,磁分离器的排水孔与微电解填料筒的进水口相连,微电解填料筒的出水口连接生物接触氧化池的进水口,生物接触氧化池的出水口连接活性炭过滤器的进口,活性炭过滤器的出口与回水池连接,微电解填料筒内位于进水口的上方由下自上依次设有微电解填料过滤层、生物填料过滤层及高密度纤维丝滤层。
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 and remove organic matter in water. The sewage has good biochemical properties and can be fully recycled in production to realize zero sewage discharge to the outside world. Advanced discharge treatment system, including sump, filter roller sieve machine, stirring reaction tower, magnetic separator, micro-electrolysis packing cylinder, biological contact oxidation tank, activated carbon filter and return pool, the outlet of the sump is connected to the inlet of the filter roller sieve machine , the outlet of the filter roller sieving machine is connected to the inlet of the stirring reaction tower, the outlet of the stirring reaction tower 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-electrolysis packing cylinder, and the water outlet of the micro-electrolysis packing cylinder is connected to the biological The water inlet of the contact oxidation tank, the water outlet of the biological contact oxidation tank is connected to the inlet of the activated carbon filter, and the outlet of the activated carbon filter is connected to the return pool. Packing filter layer, biological filler filter layer and high-density fiber silk filter layer.
Description
技术领域 technical field
本实用新型涉及一种污水处理系统,尤其是涉及污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 sewage. 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,本实用新型提供一种结构设计合理、能有效降解水中致色物质、去除水中有机物的,污水可生化性好的,可全部回收于生产,实现对外零排放的污水零排放深度处理系统。 Therefore, in view of the above problems, the utility model provides a kind of reasonable structure design, which can effectively degrade the color-causing substances in the water, remove the organic matter in the water, the sewage has good biodegradability, can be completely recycled in production, and realize zero discharge of sewage to the outside world. 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:污水零排放深度处理系统,包括集水池、过滤滚筛机、搅拌反应塔、磁分离器、微电解填料筒、生物接触氧化池、活性炭过滤器及回水池,所述集水池的出口连接过滤滚筛机的进口,所述过滤滚筛机的出口连接搅拌反应塔的进口,所述搅拌反应塔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填料筒的进水口相连,所述微电解填料筒的出水口连接生物接触氧化池的进水口,所述生物接触氧化池的出水口连接活性炭过滤器的进口,所述活性炭过滤器的出口与回水池连接, 所述微电解填料筒内位于进水口的上方由下自上依次设有微电解填料过滤层、生物填料过滤层及高密度纤维丝滤层。 In order to achieve the above-mentioned purpose, the utility model is realized through the following technical solutions: sewage zero-discharge advanced treatment system, including sump, filter roller sieve machine, stirring reaction tower, magnetic separator, micro-electrolysis packing cylinder, biological contact oxidation pool, Activated carbon filter and return pool, the outlet of the sump is connected to the inlet of the filter roller sieve machine, the outlet of the filter roller sieve machine is connected to the inlet of the stirring reaction tower, and the outlet of the stirring reaction tower is connected to the inlet of the magnetic separator. The drainage hole of the magnetic separator is connected to the water inlet of the micro-electrolysis packing cylinder, the water outlet of the micro-electrolysis packing cylinder is connected to the water inlet of the biological contact oxidation tank, and the water outlet of the biological contact oxidation tank is connected to the inlet of the activated carbon filter , the outlet of the activated carbon filter is connected to the backwater pool, and the micro-electrolysis packing cylinder is located above the water inlet, and is sequentially provided with a micro-electrolysis packing filter layer, a biological filler filter layer and a high-density fiber silk filter layer from bottom to top. the
进一步改进的是:所述微电解填料过滤层包括设于微电解填料筒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-electrolysis filler includes a cylinder body arranged on the inner wall of the circumference of the micro-electrolysis filler tube, the micro-electrolysis filler is arranged in the cylinder body, and the upper part and the lower part of the cylinder body are respectively set There are filter plates, and water-through micropores are evenly distributed on each of the filter plates. the
进一步改进的是:所述微电解填料为铁碳微电解填料。 A further improvement is: the micro-electrolytic filler is an iron-carbon micro-electrolytic filler. the
进一步改进的是:所述生物接触氧化池内下部铺设有气管,所述气管上均布有出气孔,所述气管的一端伸出池外与风机相连,所述生物接触氧化池内位于气管的出气口上部设有活性污泥填料层。 It is further improved that a trachea is laid on the lower part of the biological contact oxidation tank, and air outlets are uniformly distributed on the trachea, and one end of the trachea extends out of the tank to connect with a fan, and the air outlet of the trachea is located in the biological contact oxidation tank The upper part is provided with an activated sludge filler layer. the
进一步改进的是:所述搅拌反应塔包括搅拌塔及设于搅拌塔内的搅拌装置,所述搅拌装置包括搅拌轴及均布于搅拌轴圆周外侧的搅拌叶片,所述各搅拌叶片的下部还分别设有拨动杆。 A further improvement is: the stirring reaction tower includes a stirring tower and a stirring device arranged in the stirring tower, the stirring device includes a stirring shaft and stirring blades uniformly distributed on the outside of the stirring shaft circumference, and the lower part of each stirring blade is also There are toggle levers respectively. the
进一步改进的是:所述搅拌反应塔与磁分离器之间设有将搅拌反应塔内泥水抽往磁分离器的抽水泵,所述搅拌反应塔的底部还设有控制阀门。 A further improvement is that: a pump for pumping muddy water in the stirred reaction tower to the magnetic separator is provided between the stirred reaction tower and the magnetic separator, and a control valve is also provided at the bottom of the stirred reaction tower. the
进一步改进的是:所述磁分离器与微电解填料筒之间设有将磁分离器分离出来的污水打入微电解填料筒的水泵。 A further improvement is that: a water pump is provided between the magnetic separator and the micro-electrolysis packing cylinder to pump the sewage separated by the magnetic separator into the micro-electrolysis packing cylinder. the
通过采用前述技术方案,本实用新型的有益效果是:本实用新型污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经过滤滚筛机初步过滤后抽入搅拌反应塔,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,加药后,充分搅拌反应后,加入磁粉及絮凝剂,然后静置处理,静置处理后打开搅拌反应塔的阀门,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填料筒内进一步处理,从而降解废水中致色物质及悬浮物SS和COD,经微电解填料筒进一步微电解处理后的污水排入生物接触氧化池内,降解水中的致色物质、去除水中悬浮物,经生物接触氧化池处理后污水再经活性炭过滤器进一步过滤后达标排放或进入回水池循环利用。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 sewage 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 filtered and rolled After preliminary filtration by the sieve machine, it is pumped into the stirring reaction tower, and the agents that can complete the sedimentation of chromium, cyanide and heavy metals in the mud water are added in sequence. After treatment, open the valve of the stirring reaction tower, pump the sludge into the magnetic separator for mud-water separation treatment, and after the separation treatment, pump the supernatant in the magnetic separator into the micro-electrolysis packing cylinder for further treatment, thereby degrading the color-causing substances in the wastewater And suspended solids SS and COD, the sewage after further micro-electrolysis treatment by the micro-electrolytic packing cylinder is discharged into the biological contact oxidation tank to degrade the color-causing substances in the water and remove the suspended solids in the water. After being treated by the biological contact oxidation tank, the sewage is filtered by activated carbon After being further filtered by the filter, it is discharged up to the standard or enters the backwater pool for recycling. Its structural design is reasonable, the treatment process steps are simple, it can effectively degrade the color-causing substances in water, the removal rate of organic matter in water is high, and the sewage has good biodegradability. It can effectively treat papermaking sewage, minimize the pollution to the environment, and make it Meet the sewage discharge standard and improve the 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,本实施例公开一种污水零排放深度处理系统,包括集水池1、过滤滚筛机2、搅拌反应塔3、磁分离器4、微电解填料筒5、生物接触氧化池6、活性炭过滤器7及回水池8,所述集水池1的出口连接过滤滚筛机2的进口,所述过滤滚筛机2的出口连接搅拌反应塔3的进口,所述搅拌反应塔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,充分搅拌反应后,然后加入磁粉及絮凝剂,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,所述搅拌反应塔3的出口连接磁分离器4进口, 磁分离器4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4的排水孔与微电解填料筒5的进水口相连,所述微电解填料筒5的出水口连接生物接触氧化池6的进水口,所述生物接触氧化池6内下部铺设有气管61,所述气管61上均布有出气孔,所述气管61的一端伸出池外与风机62相连,所述生物接触氧化池6内位于气管61的出气口上部设有活性污泥填料层63,所述生物接触氧化池6的出水口64连接活性炭过滤器7的进口,所述活性炭过滤器7的出口与回水池8连接,所述微电解填料筒5内位于进水口的上方由下自上依次设有微电解填料过滤层51、生物填料过滤层52及高密度纤维丝滤层53。所述微电解填料过滤层51包括设于微电解填料筒5圆周内侧壁上的圆柱筒体、所述圆柱筒体内设有铁碳微电解填料,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。本新型污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;生物填料过滤层可进一步提高降解能力,去除水中悬浮物,提高污水有机物的去除率,使废水中的COD可达标排放。高密度纤维丝滤层的空隙多、比表面积大,具有机械截流的作用,可对水进行净化处理、截流水中的悬浮物及生物絮体,保证出水质量。
Referring to Fig. 1, this embodiment discloses a sewage zero-discharge advanced treatment system, including a sump 1, a filter roller sieve machine 2, a stirring reaction tower 3, a magnetic separator 4, a
所述搅拌反应塔3包括搅拌塔及设于搅拌塔内的搅拌装置,所述搅拌装置包括搅拌轴及均布于搅拌轴圆周外侧的搅拌叶片,所述各搅拌叶片的下部还分别设有拨动杆。 The stirring reaction tower 3 comprises a stirring tower and a stirring device located in the stirring tower, the stirring device comprises a stirring shaft and stirring blades uniformly distributed on the outside of the stirring shaft circumference, and the bottom of each stirring blade is respectively provided with a dial moving rod. the
所述搅拌反应塔3与磁分离器4之间设有将搅拌反应塔内泥水抽往磁分离器的抽水泵,所述搅拌反应塔的底部还设有控制阀门。 A pump for pumping muddy water in the stirred reaction tower to the magnetic separator is provided between the stirred reaction tower 3 and the magnetic separator 4, and a control valve is also provided at the bottom of the stirred reaction tower. the
所述磁分离器4与微电解填料筒5之间设有将磁分离器分离出来的污水打入微电解填料筒的水泵。
A water pump is provided between the magnetic separator 4 and the
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
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103816703A (en) * | 2014-02-26 | 2014-05-28 | 明圣化工机械(南通)有限公司 | Sewage treatment device |
| CN105347555A (en) * | 2015-11-18 | 2016-02-24 | 苏浩强 | Waste liquid processing system suitable for electroplating waste liquid |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103816703A (en) * | 2014-02-26 | 2014-05-28 | 明圣化工机械(南通)有限公司 | Sewage treatment device |
| CN105347555A (en) * | 2015-11-18 | 2016-02-24 | 苏浩强 | Waste liquid processing system suitable for electroplating waste liquid |
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