CN205527842U - Special air supporting water treatment facilities of organic waste water - Google Patents
Special air supporting water treatment facilities of organic waste water Download PDFInfo
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- CN205527842U CN205527842U CN201620258903.4U CN201620258903U CN205527842U CN 205527842 U CN205527842 U CN 205527842U CN 201620258903 U CN201620258903 U CN 201620258903U CN 205527842 U CN205527842 U CN 205527842U
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Abstract
一种有机废水专用气浮水处理装置,属于有机废水专用气浮水处理装置。由池外储药罐、多孔加药器和气浮处理池构成,其特征是所述池外储药罐由聚合氯化铝和聚丙烯酰胺两个絮凝剂储罐;多孔加药器是连通池外储药罐向气浮处理池内混合加药的均距多孔排管;气浮处理池由上挡板、下挡板、搅拌器、进气排管、滤渣机、排渣口、隔板、排泥口、清水出口构成。与已知技术比较本实用新型去掉了分别加药的预混搅拌池,将该功能直接设计在气浮池中,这样既减少了占地面积,又提高了工作效率。
The utility model relates to a special air flotation water treatment device for organic waste water, which belongs to the special air flotation water treatment device for organic waste water. It consists of a medicine storage tank outside the pool, a porous dosing device and an air flotation treatment tank, and is characterized in that the medicine storage tank outside the pool is composed of two flocculant storage tanks, polyaluminum chloride and polyacrylamide; the porous dosing device is a connected pool The uniformly spaced porous pipes for mixing and adding medicine from the external medicine storage tank to the air flotation treatment tank; Consists of mud discharge outlet and clean water outlet. Compared with the known technology, the utility model removes the premixed stirring tank for adding medicine separately, and directly designs this function in the air flotation tank, which not only reduces the occupied area, but also improves the work efficiency.
Description
技术领域technical field
本实用新型涉及一种有机废水专用气浮水处理装置。The utility model relates to a special air flotation water treatment device for organic waste water.
背景技术Background technique
目前,通用型气浮设备的设计核心基本是依据《工业废水处理技术》(邹家庆 著)书中第四章第二节中的浮选法处理废水的技术。根据该书所说,大多数的设备按如下方式工作:将溶解好的药品经加药泵打进预混池内,在预混池中经搅拌混合进行絮凝,待废水产生污泥,泥水混合物经管路进入气浮池通过浮选法进行固液分离得到清水。该方法已经被广泛的应用,但是该设备应用在有机废水的处理中会有如下的缺点:At present, the design core of general-purpose air flotation equipment is basically based on the flotation method in the second section of Chapter 4 of the book "Industrial Wastewater Treatment Technology" (Zou Jiaqing). According to the book, most of the equipment works as follows: the dissolved medicine is pumped into the premix tank through the dosing pump, and flocculated by stirring and mixing in the premix tank. The road enters the air flotation tank for solid-liquid separation by flotation to obtain clean water. This method has been widely used, but the application of this equipment in the treatment of organic wastewater has the following disadvantages:
1.有机废水一般化学需氧量值高,进入气浮设备之前需要添絮凝剂加聚合氯化铝(PAC)和聚丙烯酰胺(PAM)。该设计需要配有2个加药的预混池及2台搅拌机分别加入PAC和PAM进行絮凝。 因此操作繁琐,占地面积大。如果在气浮池直接添加絮凝剂,又会造成混合不均匀,絮凝效果差的缺陷。1. Organic wastewater generally has a high chemical oxygen demand value, and flocculants, polyaluminum chloride (PAC) and polyacrylamide (PAM) need to be added before entering the air flotation equipment. The design needs to be equipped with 2 pre-mixing tanks for dosing and 2 mixers to add PAC and PAM respectively for flocculation. Therefore, the operation is complicated and the floor area is large. If the flocculant is directly added to the air flotation tank, it will cause uneven mixing and poor flocculation effect.
2.有机废水出泥量大,在用常规的气浮设备时,泥水混合物管路内会遗留一定的絮凝物,运转一段时间后就会堵塞管路,所以要定期的清理管路。来回拆卸管路是非常繁琐的过程。另外当设备停止不用时,气浮池底部会沉淀一些絮凝物,每周需将池内净化后的水抽出,由操作人员进入池内,将底部沉淀物清理干净,因此使用起来需要定期检修维护。2. The amount of sludge produced by organic wastewater is large. When using conventional air flotation equipment, a certain amount of flocs will remain in the mud-water mixture pipeline, which will block the pipeline after a period of operation, so the pipeline should be cleaned regularly. Going back and forth to remove the tubing is a very tedious process. In addition, when the equipment is not in use, some flocs will be deposited at the bottom of the air flotation tank. The purified water in the tank needs to be pumped out every week, and the operator enters the tank to clean up the sediment at the bottom. Therefore, regular maintenance is required for use.
发明内容Contents of the invention
本实用新型的目的是将有机废水处理的操作步骤简化,克服管路堵塞,提高工作效率,并减少占地面积。本实用新型的技术方案是设计一种有机废水专用气浮水处理装置,该装置由池外储药罐、多孔加药器和气浮处理池构成,其中池外储药罐包括聚合氯化铝和聚丙烯酰胺两个絮凝剂储罐;多孔加药器是连通池外储药罐向气浮处理池内混合加药的均距多孔排管;气浮处理池由上挡板、下挡板、搅拌器、滤渣机、进气排管、排渣口、隔板、排泥口、清水出口构成。The purpose of the utility model is to simplify the operation steps of organic waste water treatment, overcome pipeline blockage, improve work efficiency, and reduce occupied area. The technical solution of the utility model is to design a special air flotation water treatment device for organic wastewater, which is composed of a storage tank outside the pool, a porous dosing device and an air flotation treatment tank, wherein the storage tank outside the pool includes polyaluminum chloride and poly There are two flocculant storage tanks for acrylamide; the porous dosing device is an evenly spaced porous pipe that connects the storage tank outside the tank to mix and add medicine to the air flotation treatment tank; the air flotation treatment tank consists of an upper baffle, a lower baffle, and an agitator , Residue filter machine, intake pipe, slag outlet, clapboard, mud outlet, clean water outlet.
与已知技术比较其积极效果是本实用新型能够保证药剂直接加进气浮处理池内与废水快速充分的接触。在进气排管上方安装多孔加药器及一套搅拌器,有利于充分混合。当絮凝出现时,大部分污泥附着在气泡上,跟随气泡上升至气浮处理池液面上,被上面的刮渣机刮走。本设备在浮选池底部安装了排泥管路,小部分污泥沉降到底部可被排泥管路排出,大大减少了池内清理浮选池底部污泥的工作量,这样既减少了占地面积,又提高了工作效率。Compared with the known technology, the positive effect of the utility model is that the utility model can ensure that the medicament can be directly added into the air-float treatment tank to quickly and fully contact with the waste water. Install a multi-hole dosing device and a set of agitators above the intake exhaust pipe, which is conducive to full mixing. When flocculation occurs, most of the sludge adheres to the air bubbles, follows the air bubbles to rise to the liquid surface of the air flotation treatment tank, and is scraped away by the slag scraper above. The equipment is equipped with a sludge discharge pipeline at the bottom of the flotation tank, and a small part of the sludge can be discharged by the sludge discharge pipeline when it settles to the bottom, which greatly reduces the workload of cleaning the sludge at the bottom of the flotation tank in the tank, which not only reduces the occupied area area, and improved work efficiency.
附图说明Description of drawings
图1是本实用新型结构示意图Fig. 1 is a structural representation of the utility model
图2为多孔加药器的示意图Figure 2 is a schematic diagram of a porous dosing device
其中1、废水进水口 2、多孔加药器 3、进气排管 4、刮渣机 5、排渣口1. Waste water inlet 2. Porous dosing device 3. Air intake pipe 4. Slag scraper 5. Slag discharge port
6、清水出口7、排泥口 8、聚合氯化铝储罐 9、聚丙烯酰胺储罐 10、搅拌器6. Clean water outlet 7, mud outlet 8, polyaluminum chloride storage tank 9, polyacrylamide storage tank 10, agitator
11、气浮处理池 12、隔板 13、上档板 14、下档板 。11. Air flotation treatment pool 12. Separator 13. Upper baffle 14. Lower baffle.
具体实施方式detailed description
以下结合附图详细说明本实用新型的结构及使用方法:Below in conjunction with accompanying drawing, describe structure of the present utility model and using method in detail:
如图所示本实用新型由池外储药罐(8)(9)、多孔加药器(2)、气浮处理池(11)构成。其中池外药罐包括聚合氯化铝和聚丙烯酰胺两个絮凝剂储罐(8)(9);多孔加药器(2)是连通池外储药罐(8)(9)向气浮处理池(11)内混合加药的均距多孔排管;气浮处理池(11)由上挡板(13)、下挡板(14)、搅拌器(10)、进气排管(3)、滤渣机(4)、排渣口(5)、隔板(12)、排泥口(7)、清水出口(6)构成。运行时,有机废水经废水进水口(1)进入气浮处理池(11)。来自多孔加药器(2)的聚合氯化铝和聚丙烯酰胺与经进气排管(3)里出来的气泡搅拌,充分混合发生反应。絮凝产生大量的污泥,这些污泥随着气泡的上升流到刮渣机(4),污泥经刮渣机分离到排渣口(5),分离出的清水由清水出口(6)流出。操作人员定期打开排泥口(7)来排出残留在通过进气排管(3)附近的污泥。As shown in the figure, the utility model is composed of medicine storage tank (8) (9) outside the pool, porous medicine dosing device (2), and air flotation treatment pool (11). Among them, the medicine tank outside the pool includes two flocculant storage tanks (8) (9) of polyaluminum chloride and polyacrylamide; the porous dosing device (2) is connected to the medicine storage tank (8) (9) outside the pool to the air flotation The uniformly spaced porous pipes for mixing and dosing in the treatment tank (11); the air flotation treatment tank (11) consists of an upper baffle (13), a lower baffle (14), an agitator (10), and an air intake pipe (3 ), residue filter (4), slag outlet (5), clapboard (12), mud outlet (7), clear water outlet (6). During operation, the organic waste water enters the air flotation treatment tank (11) through the waste water inlet (1). The polyaluminium chloride and polyacrylamide from the porous dosing device (2) are stirred with the air bubbles coming out of the air intake pipe (3) and fully mixed to react. Flocculation produces a large amount of sludge, which flows to the slag scraper (4) as the air bubbles rise, and the sludge is separated by the slag scraper to the slag discharge port (5), and the separated clean water flows out from the clean water outlet (6) . The operator periodically opens the sludge outlet (7) to discharge the sludge remaining near the intake pipe (3).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620258903.4U CN205527842U (en) | 2016-03-31 | 2016-03-31 | Special air supporting water treatment facilities of organic waste water |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620258903.4U CN205527842U (en) | 2016-03-31 | 2016-03-31 | Special air supporting water treatment facilities of organic waste water |
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| CN205527842U true CN205527842U (en) | 2016-08-31 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620258903.4U Expired - Lifetime CN205527842U (en) | 2016-03-31 | 2016-03-31 | Special air supporting water treatment facilities of organic waste water |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107697971A (en) * | 2017-09-30 | 2018-02-16 | 北京海绵城市建设工程有限公司 | One kind is without air saturator type efficient air-floating apparatus |
| CN113200629A (en) * | 2021-06-17 | 2021-08-03 | 中冶京诚工程技术有限公司 | Flotation device and water body purification integrated system |
| CN113428927A (en) * | 2021-07-22 | 2021-09-24 | 燕山大学 | Method for removing acetaminophen in pharmaceutical wastewater |
-
2016
- 2016-03-31 CN CN201620258903.4U patent/CN205527842U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107697971A (en) * | 2017-09-30 | 2018-02-16 | 北京海绵城市建设工程有限公司 | One kind is without air saturator type efficient air-floating apparatus |
| CN113200629A (en) * | 2021-06-17 | 2021-08-03 | 中冶京诚工程技术有限公司 | Flotation device and water body purification integrated system |
| CN113428927A (en) * | 2021-07-22 | 2021-09-24 | 燕山大学 | Method for removing acetaminophen in pharmaceutical wastewater |
| CN113428927B (en) * | 2021-07-22 | 2022-08-30 | 燕山大学 | Method for removing acetaminophen in pharmaceutical wastewater |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20160831 |
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| CX01 | Expiry of patent term |