CN201400629Y - Floor processing wastewater treatment and reuse system - Google Patents
Floor processing wastewater treatment and reuse system Download PDFInfo
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- CN201400629Y CN201400629Y CN2009203025359U CN200920302535U CN201400629Y CN 201400629 Y CN201400629 Y CN 201400629Y CN 2009203025359 U CN2009203025359 U CN 2009203025359U CN 200920302535 U CN200920302535 U CN 200920302535U CN 201400629 Y CN201400629 Y CN 201400629Y
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- 238000004065 wastewater treatment Methods 0.000 title abstract description 10
- 238000004062 sedimentation Methods 0.000 claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000002351 wastewater Substances 0.000 claims abstract description 29
- 238000006243 chemical reaction Methods 0.000 claims abstract description 26
- 239000010802 sludge Substances 0.000 claims abstract description 26
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 24
- 239000000945 filler Substances 0.000 claims abstract description 14
- 239000000725 suspension Substances 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 8
- 238000005273 aeration Methods 0.000 claims description 18
- 239000003814 drug Substances 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims 2
- 230000003647 oxidation Effects 0.000 abstract description 17
- 239000000126 substance Substances 0.000 abstract description 14
- 239000007788 liquid Substances 0.000 abstract description 5
- 239000007787 solid Substances 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012476 oxidizable substance Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 239000006228 supernatant Substances 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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- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型涉及一种废水处理系统,尤其是涉及一种地板加工废水处理及回用系统。其主要是解决现有技术所存在的废水池的容积量较小,所处理的污水量较小,并且其在处理污泥较多的废水时,液体不容易与固体分离开来等的技术问题。本实用新型包括预曝调节池,预曝调节池上设有水泵,水泵连通有反应初沉池,反应初沉池连通有药剂槽,反应初沉池的底部设有第一沉淀区,反应初沉池上部连通有接触氧化池,接触氧化池的池内连接有生物悬浮填料,接触氧化池通过管路连接有二次沉淀池,二次沉淀池底部设有第二沉淀区,第一沉淀区与第二沉淀区都通过污泥管连接污泥干化池,二次沉淀池通过管路连通有过滤池,过滤池通过水管连接清水存储池。
The utility model relates to a wastewater treatment system, in particular to a floor processing wastewater treatment and reuse system. It is mainly to solve the technical problems of the existing technology that the volume of the waste water pool is small, the amount of sewage treated is small, and when the waste water with a lot of sludge is treated, the liquid is not easy to separate from the solid, etc. . The utility model comprises a pre-exposure adjustment tank, on which a water pump is arranged, the water pump is connected with a reaction primary sedimentation tank, the reaction primary sedimentation tank is connected with a chemical tank, the bottom of the reaction primary sedimentation tank is provided with a first sedimentation area, and the reaction primary sedimentation tank is connected with a chemical tank. The upper part of the pool is connected with a contact oxidation tank, and the tank of the contact oxidation tank is connected with a biological suspension filler. The contact oxidation tank is connected with a secondary sedimentation tank through a pipeline, and the bottom of the secondary sedimentation tank is provided with a second sedimentation zone. The secondary sedimentation area is connected to the sludge drying tank through the sludge pipe, the secondary sedimentation tank is connected to the filter tank through the pipeline, and the filter tank is connected to the clear water storage tank through the water pipe.
Description
技术领域 technical field
本实用新型涉及一种废水处理系统,尤其是涉及一种对地板加工废水处理及回用系统等结构的改良。The utility model relates to a waste water treatment system, in particular to an improvement on the structure of the floor processing waste water treatment and reuse system.
背景技术 Background technique
地板加工产生的废水由于具有一些生化物质,因此目前普通的废水处理方法很难处理这类废水。中国专利公开了一种组合式废水处理装置(授权公开号:CN 2374542Y),其由七个相连通的单元池组成,单元池的排列顺序是缺氧池、预曝池、初沉池、曝气池、二沉池、污泥池、生物滤池,预曝池和曝气池底部设有用于充气的空气管,曝气池中有半软性纤维填料和活性污泥,生物滤池是自下而上的进水,滤料为炉渣或纤维球。但这种废水装置的由于设置成一个矩形的区域,所处理的污水量较小,并且其在处理污泥较多的废水时,液体不容易与固体分离开来。The wastewater produced by floor processing has some biochemical substances, so the current common wastewater treatment methods are difficult to treat this type of wastewater. A Chinese patent discloses a combined wastewater treatment device (authorized publication number: CN 2374542Y), which consists of seven connected unit pools, and the sequence of the unit pools is anoxic pool, pre-aeration tank, primary sedimentation tank, exposure tank Air tanks, secondary settling tanks, sludge tanks, biological filters, air pipes for aeration are provided at the bottom of pre-aeration tanks and aeration tanks, semi-soft fiber filler and activated sludge are in the aeration tanks, and biological filters are The water is fed from bottom to top, and the filter material is slag or fiber ball. However, since this waste water device is arranged in a rectangular area, the amount of sewage treated is small, and when it treats waste water with a lot of sludge, the liquid is not easy to separate from the solid.
实用新型内容 Utility model content
本实用新型需要解决的技术问题是提供一种地板加工废水处理及回用系统,其主要是解决现有技术所存在的废水池的容积量较小,所处理的污水量较小,并且其在处理污泥较多的废水时,液体不容易与固体分离开来等的技术问题。The technical problem to be solved by the utility model is to provide a floor processing wastewater treatment and reuse system, which mainly solves the problem that the volume of the wastewater pool in the prior art is small, the amount of sewage treated is small, and its When dealing with wastewater with a lot of sludge, it is difficult to separate the liquid from the solid and other technical problems.
本实用新型的上述技术问题主要是通过下述技术方案得以解决的:The above-mentioned technical problems of the utility model are mainly solved by the following technical solutions:
本实用新型的地板加工废水处理及回用系统,包括可存放地板加工废水的预曝调节池,预曝调节池上设有水泵,其特征在于所述的水泵通过水管连通有反应初沉池,反应初沉池还通过药剂管连通有药剂槽,反应初沉池的底部设有第一沉淀区,反应初沉池上部通过集水槽连通有接触氧化池,接触氧化池的池内连接有若干生物悬浮填料,接触氧化池通过管路连接有二次沉淀池,二次沉淀池底部设有第二沉淀区,第一沉淀区与第二沉淀区都通过污泥管连接污泥干化池,二次沉淀池通过管路连通有过滤池,过滤池通过水管连接清水存储池。预曝调节池、污泥干化池、清水存储池可以埋于地下,药剂槽与水泵可以置于预曝调节池处,药剂槽内的药剂可注入到反应初沉池,反应初沉池内部的废水与药剂反应生成絮凝体,絮凝体在反应初沉池内静置沉淀,然后除去絮凝体。接触氧化池采用结构简单、操作简便的推流式结构,接触氧化池内部的生物悬浮填料,当系统运行到一段时间后,接触氧化池内将有大量的活性污泥,大部分污泥以生物膜的形式附着生长在生物悬浮填料上,用生物膜法相对来说可以用来处理浓度较高的废水,具有较强的抗冲击负荷能力。过滤池内可以设置多层过滤层,其可对水质进行净化,最后进入清水存储池的水达到了回用的标准,可以外排使用。The floor processing wastewater treatment and reuse system of the present utility model includes a pre-exposure adjustment tank capable of storing floor processing wastewater, and a water pump is arranged on the pre-exposure adjustment tank, which is characterized in that the water pump is connected to a reaction primary sedimentation tank through a water pipe, and the reaction The primary sedimentation tank is also connected with a chemical tank through a chemical pipe. The bottom of the reaction primary sedimentation tank is provided with a first sedimentation zone. The upper part of the reaction primary sedimentation tank is connected with a contact oxidation tank through a water collection tank. The tank of the contact oxidation tank is connected with a number of biological suspension fillers. , the contact oxidation tank is connected to the secondary sedimentation tank through pipelines, the second sedimentation zone is set at the bottom of the secondary sedimentation tank, the first sedimentation zone and the second sedimentation zone are connected to the sludge drying tank through the sludge pipe, and the secondary sedimentation The pool is connected with a filter pool through a pipeline, and the filter pool is connected with a clear water storage pool through a water pipe. The pre-exposure adjustment tank, sludge drying tank, and clean water storage tank can be buried underground. The chemical tank and water pump can be placed in the pre-exposure adjustment tank. The chemical in the chemical tank can be injected into the reaction primary sedimentation tank, and the reaction primary sedimentation tank The waste water reacts with the chemical to form flocs, which are left to settle in the reaction primary sedimentation tank, and then the flocs are removed. The contact oxidation tank adopts a plug-flow structure with simple structure and easy operation, and the biological suspension filler inside the contact oxidation tank. When the system runs for a period of time, there will be a large amount of activated sludge in the contact oxidation tank, most of which are formed by biofilm The form attaches to and grows on the biological suspension filler, and the biofilm method can be used to treat wastewater with a relatively high concentration, and has a strong ability to resist impact loads. Multi-layer filter layers can be set in the filter tank, which can purify the water quality, and finally the water entering the clear water storage tank has reached the reuse standard and can be used outside.
作为优选,所述的预曝调节池与接触氧化池的底部设有穿孔曝气管,穿孔曝气管通过风管连接有风机。穿孔曝气管为ABS穿孔曝气管,一方面可以对废水进行初步的氧化反应,去除废水中部分易氧化物质,另一方面通过曝气可以均化废水的水质,使废水水质能相对地保持稳定。As a preference, the bottom of the pre-aeration adjustment tank and the contact oxidation tank is provided with a perforated aeration pipe, and the perforated aeration pipe is connected with a fan through an air pipe. The perforated aeration tube is an ABS perforated aeration tube. On the one hand, it can perform a preliminary oxidation reaction on the wastewater to remove some easily oxidizable substances in the wastewater. On the other hand, it can homogenize the water quality of the wastewater through aeration, so that the quality of the wastewater can be relatively maintained Stablize.
作为优选,所述的反应初沉池的进口处设有搅拌器,搅拌器连接有电机。搅拌器可以将废水进行固液分散,重量较重的污泥则会沉淀到第一沉淀区内,重量较轻的水则会浮于上方。As a preference, a stirrer is provided at the inlet of the reaction primary sedimentation tank, and the stirrer is connected with a motor. The agitator can disperse the wastewater into solid and liquid, and the heavy sludge will settle into the first settling zone, while the light water will float on top.
作为优选,所述的生物悬浮填料成矩阵排列,其悬挂在接触氧化池内。生物悬浮填料可以排布为5~10列,每列均布有5~10个填料。As a preference, the biological suspension filler is arranged in a matrix, which is suspended in the contact oxidation tank. Biological suspension fillers can be arranged in 5~10 rows, each row has 5~10 fillers evenly distributed.
因此,本实用新型具有废水池的容积量较大,所处理的污水量较大,并且其在处理污泥较多的废水时,采用搅拌器,使得液体比较容易与固体分离开来,结构简单、合理等特点。Therefore, the utility model has a larger volume of the waste water tank and a larger amount of sewage to be treated, and when treating waste water with a lot of sludge, the agitator is used to make it easier to separate the liquid from the solid, and the structure is simple , reasonable and other characteristics.
附图说明 Description of drawings
附图1是本实用新型的一种结构示意图。Accompanying drawing 1 is a kind of structural representation of the utility model.
图中零部件、部位及编号:预曝调节池1、水泵2、水管3、反应初沉池4、药剂槽5、第一沉淀区6、集水槽7、接触氧化池8、生物悬浮填料9、二次沉淀池10、第二沉淀区11、污泥管12、污泥干化池13、过滤池14、清水存储池15、穿孔曝气管16、风管17、风机18、搅拌器19、电机20、药剂管21。Parts, parts and numbers in the figure: pre-exposure adjustment tank 1, water pump 2, water pipe 3, reaction primary sedimentation tank 4, chemical tank 5, first sedimentation zone 6, water collection tank 7,
具体实施方式 Detailed ways
下面通过实施例,并结合附图,对本实用新型的技术方案作进一步具体的说明。The technical solutions of the present utility model will be further specifically described below through the embodiments and in conjunction with the accompanying drawings.
实施例:本例的地板加工废水处理及回用系统,如图1,有一个存放地板加工废水的预曝调节池1,预曝调节池处设有药剂槽5与水泵2,水泵的进口处通过水管3伸入预曝调节池内。水泵出口处通过水管3连接有反应初沉池4,反应初沉池4通过药剂管21连通药剂槽5。反应初沉池4的进口处设有搅拌器19,搅拌器连接电机20并由其驱动。搅拌器由转轴以及桨叶组成。反应初沉池4的下方设有第一沉淀区6,第一沉淀区6通过污泥管12连通污泥干化池13。反应初沉池4上部通过集水槽7连通有接触氧化池8,接触氧化池的池内悬挂有成矩阵排列的生物悬浮填料9,接触氧化池8与预曝调节池1的底部都设有穿孔曝气管16,穿孔曝气管通过风管17连接风机18。接触氧化池8通过管路连接有二次沉淀池10,二次沉淀池底部设有第二沉淀区11,第二沉淀区通过污泥管12连接污泥干化池13,二次沉淀池通过管路连通有过滤池14,过滤池通过水管连接清水存储池15。Embodiment: The floor processing wastewater treatment and reuse system of this example, as shown in Figure 1, has a pre-exposure adjustment tank 1 for storing floor processing wastewater. The pre-exposure adjustment tank is provided with a chemical tank 5 and a water pump 2, and the inlet of the water pump Extend into the pre-exposure adjustment tank through the water pipe 3. The outlet of the water pump is connected to the reaction primary sedimentation tank 4 through the water pipe 3, and the reaction primary sedimentation tank 4 is connected to the chemical tank 5 through the chemical pipe 21. An
使用时,车间生产混合废水经收集后进入到预曝调节池1内,池底的穿孔曝气管16一方面可以对废水进行初步的氧化反应,去除废水中部分易氧化物质,另一方面通过曝气可以均化废水的水质,使废水水质能相对地保持稳定;然后由水泵2提升送至反应初沉池4,通过在反应池内加药剂反应生成絮凝体,然后在沉淀池内静置沉淀除去絮凝体。上清液经集水槽7收集后自流进入接触氧化池8,当设施运行到一段时间后,池内将有大量的活性污泥,大部分污泥以生物膜的形式附着生长在生物悬浮填料9上,用生物膜法相对来说可以用来处理浓度较高的废水,具有较强的抗冲击负荷能力。生化处理后的出水自流进入二次沉淀池10进行泥水分离,然后进入过滤池14,使水质得到进一步净化,达到回用标准,出水再进入到清水存储池15备用。反应初沉池4及二次沉淀池10内的污泥定期通过静水头压送至污泥干化池,干化的污泥需运至专业的固废处理公司进行处置。When in use, the mixed wastewater produced in the workshop enters the pre-aeration regulating tank 1 after being collected. Aeration can homogenize the water quality of the wastewater, so that the water quality of the wastewater can be kept relatively stable; then it is lifted by the water pump 2 to the reaction primary sedimentation tank 4, and the flocs are formed by adding chemicals in the reaction tank, and then left to settle in the sedimentation tank to remove flocs. After the supernatant is collected by the water collection tank 7, it flows into the
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| CN2009203025359U CN201400629Y (en) | 2009-04-24 | 2009-04-24 | Floor processing wastewater treatment and reuse system |
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| CN2009203025359U CN201400629Y (en) | 2009-04-24 | 2009-04-24 | Floor processing wastewater treatment and reuse system |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805102A (en) * | 2010-05-27 | 2010-08-18 | 江门裕华皮革有限公司 | Wastewater treatment method |
| CN105439330A (en) * | 2016-01-15 | 2016-03-30 | 芜湖林诺环保科技有限公司 | Small sewage treatment device and control method thereof |
| CN106186511A (en) * | 2016-07-04 | 2016-12-07 | 宜兴市永加化工有限公司 | A kind of wastewater treatment equipment |
| CN111547888A (en) * | 2020-05-20 | 2020-08-18 | 四川省工业环境监测研究院 | Wastewater treatment device for water and soil pollution control and treatment method thereof |
| CN113248076A (en) * | 2021-04-09 | 2021-08-13 | 宁波市鄞州区水利水电勘测设计院 | Polluted city internal lake water quality purification and water ecological restoration system |
-
2009
- 2009-04-24 CN CN2009203025359U patent/CN201400629Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805102A (en) * | 2010-05-27 | 2010-08-18 | 江门裕华皮革有限公司 | Wastewater treatment method |
| CN105439330A (en) * | 2016-01-15 | 2016-03-30 | 芜湖林诺环保科技有限公司 | Small sewage treatment device and control method thereof |
| CN106186511A (en) * | 2016-07-04 | 2016-12-07 | 宜兴市永加化工有限公司 | A kind of wastewater treatment equipment |
| CN111547888A (en) * | 2020-05-20 | 2020-08-18 | 四川省工业环境监测研究院 | Wastewater treatment device for water and soil pollution control and treatment method thereof |
| CN111547888B (en) * | 2020-05-20 | 2022-03-01 | 四川省工业环境监测研究院 | Wastewater treatment device for water and soil pollution control and treatment method thereof |
| CN113248076A (en) * | 2021-04-09 | 2021-08-13 | 宁波市鄞州区水利水电勘测设计院 | Polluted city internal lake water quality purification and water ecological restoration system |
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