CN207031014U - A kind of new batch-type air-dissolving air-float equipment for separating liquid from solid - Google Patents

A kind of new batch-type air-dissolving air-float equipment for separating liquid from solid Download PDF

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CN207031014U
CN207031014U CN201720570001.9U CN201720570001U CN207031014U CN 207031014 U CN207031014 U CN 207031014U CN 201720570001 U CN201720570001 U CN 201720570001U CN 207031014 U CN207031014 U CN 207031014U
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air flotation
water inlet
separation tank
water
valve
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李福勤
赵桂峰
卜云云
文兴
崔燚
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Hebei University of Engineering
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Hebei University of Engineering
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Abstract

本实用新型提供了一种新型序批式溶气气浮固液分离装置,包括管式反应器,所述管式反应器的前端安装有管式混合器,所述管式混合器的前端连接有一条进水管的一端,所述进水管的另一端通过三通分别连接有一个加药阀和一个进水阀,所述进水阀的另一端连接有一个原水泵;所述管式反应器的后端连接一个气浮分离池的底部进水口。所述气浮分离池的内部下半部分设置有多条表面打有多排出水孔的穿孔出水管,所述穿孔出水管的一端封闭,另一端连接设置于气浮分离池外部的出水阀。本专利具有如下优点:1、气浮分离池独立设置,浮渣上升时,水流是上升或静止的,分离效率高效果好;2、采用管式混合器,创造了微气泡与混凝絮体的共聚环境,为共聚气浮创造了条件,分离更充分,且不易堵塞。

The utility model provides a novel sequencing batch type dissolved air flotation solid-liquid separation device, comprising a tubular reactor, the front end of the tubular reactor is equipped with a tubular mixer, and the front end of the tubular mixer is connected to There is one end of a water inlet pipe, the other end of the water inlet pipe is respectively connected to a dosing valve and a water inlet valve through a tee, and the other end of the water inlet valve is connected to a raw water pump; the tubular reactor The rear end of the tank is connected to the bottom water inlet of an air flotation separation tank. The inner lower half of the air flotation separation tank is provided with a plurality of perforated water outlet pipes with multiple discharge holes on the surface. One end of the perforated water outlet pipes is closed, and the other end is connected to the water outlet valve arranged outside the air flotation separation tank. This patent has the following advantages: 1. The air flotation separation tank is set independently. When the scum rises, the water flow is rising or static, and the separation efficiency is high; 2. The tube mixer is used to create micro-bubbles and coagulation flocs The perfect copolymerization environment creates conditions for the copolymerization air flotation, the separation is more sufficient, and it is not easy to block.

Description

一种新型序批式溶气气浮固液分离装置A new sequence batch type dissolved air flotation solid-liquid separation device

技术领域technical field

本实用新型涉及一种污水处理用固液分离装置,尤其是一种整体结构简单可靠,设计巧妙,反应充分,不易堵塞,分离效果好的新型序批式溶气气浮固液分离装置。The utility model relates to a solid-liquid separation device for sewage treatment, in particular to a new sequence batch type dissolved air flotation solid-liquid separation device with simple and reliable overall structure, ingenious design, sufficient reaction, not easy to be blocked, and good separation effect.

背景技术Background technique

气浮技术是一种高效的固液分离技术,广泛地运用于含油、悬浮物、高浓度有机废水的预处理中,例如炼油、机械加工、印染、造纸、农药等行业废水的处理,主要用于去除废水中比重小于或接近1的油分、乳化液以及悬浮颗粒物。与沉淀法相比,气浮法分离效率高,气浮分离能力约为沉淀分离能力的4~5倍;气浮法不断地向水中充气,具有预曝气、脱色、降低COD值和较好的氨氮降解功能;气浮上层浮渣含水率低,可减少污泥处置费用。Air flotation technology is an efficient solid-liquid separation technology, which is widely used in the pretreatment of oily, suspended solids, and high-concentration organic wastewater, such as the treatment of wastewater from oil refining, mechanical processing, printing and dyeing, papermaking, and pesticide industries. It is used to remove oil, emulsion and suspended particles whose specific gravity is less than or close to 1 in wastewater. Compared with the sedimentation method, the separation efficiency of the air flotation method is high, and the separation capacity of the air flotation method is about 4 to 5 times that of the precipitation separation method; Ammonia nitrogen degradation function; the water content of scum in the upper layer of air flotation is low, which can reduce the cost of sludge disposal.

传统气浮法种类很多,但万变不离其宗,主要包括三个过程:气泡的产生、气泡与颗粒的粘附以及絮体上浮分离。根据气泡的产生方式不同,气浮法大体分为三种:电解气浮、散气气浮和溶气气浮。其中溶气气浮法产生的气泡相对于散气气浮均匀、细小,对污染物的去除效率远远高于散气气浮,同时其在运行、操作和经济性方面比电解气浮更为方便和合理,因此应用最为广泛。There are many types of traditional air flotation methods, but they are always the same. They mainly include three processes: the generation of air bubbles, the adhesion of air bubbles and particles, and the floating and separation of flocs. According to the different ways of generating bubbles, the air flotation method is roughly divided into three types: electrolytic air flotation, diffused air flotation and dissolved air flotation. Among them, the bubbles produced by the dissolved air flotation method are uniform and fine compared with the diffused air flotation, and the removal efficiency of pollutants is much higher than that of the diffused air flotation. At the same time, it is more efficient than the electrolytic air flotation in terms of operation, operation and economy. Convenient and reasonable, so it is the most widely used.

但是,传统溶气气浮法存在以下缺点:(1)在分离区气泡粘附污染物向上流,而处理后水向下流,受水力条件、原水水质水量的影响较大,运行不稳定,分离效果远低于理论效果;(2)传统溶气气浮采用溶气释放器流道窄小且复杂,非常容易堵塞,尽管很多释放器均有冲洗措施,但效果一般均不理想;(3)传统溶气气浮反应池、接触区和分离区单独设立,占地较大;(4)传统溶气气浮反应池按沉淀池设计参数设计或无反应池,这都不满足气浮过程对反应的要求。总之,传统溶气气浮受水力条件、原水水质水量的影响较大,释放器易堵,反应程度不合理,运行不稳定,分离效果相对较差。However, the traditional dissolved air flotation method has the following disadvantages: (1) In the separation area, the air bubbles adhere to the pollutants and flow upward, while the treated water flows downward, which is greatly affected by the hydraulic conditions and the quality and quantity of raw water, and the operation is unstable. The effect is much lower than the theoretical effect; (2) The traditional dissolved air flotation adopts the narrow and complicated flow path of the dissolved air releaser, which is very easy to block. Although many releasers have flushing measures, the effect is generally not ideal; (3) The traditional dissolved air flotation reaction tank, contact area and separation area are set up separately, occupying a large area; (4) The traditional dissolved air flotation reaction tank is designed according to the design parameters of the sedimentation tank or no reaction tank, which does not meet the requirements of the air flotation process. response request. In short, traditional dissolved air flotation is greatly affected by hydraulic conditions, raw water quality and quantity, the releaser is easy to block, the degree of reaction is unreasonable, the operation is unstable, and the separation effect is relatively poor.

实用新型内容Utility model content

为解决上述问题,本实用新型提供了一种整体结构简单可靠,设计巧妙,反应充分,不易堵塞,分离效果好的新型序批式溶气气浮固液分离装置。In order to solve the above problems, the utility model provides a new sequence batch type dissolved air flotation solid-liquid separation device with simple and reliable overall structure, ingenious design, sufficient reaction, not easy to block, and good separation effect.

实现本实用新型目的的一种新型序批式溶气气浮固液分离装置,包括管式反应器,所述管式反应器的前端安装有管式混合器,所述管式混合器的前端连接有一条进水管的一端,所述进水管的另一端通过三通分别连接有一个加药阀和一个进水阀,所述进水阀的另一端连接有一个原水泵;A new sequence batch type dissolved air flotation solid-liquid separation device to achieve the purpose of this utility model, comprising a tubular reactor, the front end of the tubular reactor is equipped with a tubular mixer, the front end of the tubular mixer One end of a water inlet pipe is connected, and the other end of the water inlet pipe is respectively connected to a dosing valve and a water inlet valve through a tee, and the other end of the water inlet valve is connected to a raw water pump;

所述管式反应器的后端连接一个气浮分离池的底部进水口。The back end of the tubular reactor is connected to the bottom water inlet of an air flotation separation tank.

所述气浮分离池的内部下半部分设置有多条表面打有多排出水孔的穿孔出水管,所述穿孔出水管的一端封闭,另一端连接设置于气浮分离池外部的出水阀;所述气浮分离池的顶部左侧设置有一个液位传感器,所述气浮分离池的顶部右侧设置有一个刮渣机,所述刮渣机的底部设置有底部略低于最高液面的刮渣板;所述气浮分离池的右侧壁上、与最高液面持平的位置开有一个排渣口。The inner lower half of the air flotation separation tank is provided with a plurality of perforated water outlet pipes with multiple discharge holes on the surface, one end of the perforated water outlet pipe is closed, and the other end is connected to the water outlet valve arranged outside the air flotation separation tank; A liquid level sensor is provided on the left side of the top of the air flotation separation tank, a slag scraper is provided on the top right side of the air flotation separation tank, and a bottom slightly lower than the highest liquid level is provided at the bottom of the slag scraper. A slag scraper; a slag outlet is opened on the right side wall of the air flotation separation tank at a position equal to the highest liquid level.

所述原水泵、进水阀、加药阀、液位传感器、刮渣机、出水阀、进溶气水阀均同时连接总控箱。The raw water pump, water inlet valve, dosing valve, liquid level sensor, slag scraper, water outlet valve, and dissolved air inlet valve are all connected to the master control box at the same time.

本专利所述的一种新型序批式溶气气浮固液分离装置,待处理的原水池的原水由原水泵提升,混凝剂由加药阀进入管道混合器,流经管道反应器,溶气水通过进溶气水阀进入管道反应器,反应后的水与溶气水共同进入气浮分离池,当水位上升到最高液位时,液位传感器感应到,受总控制箱控制,停止进水、停止加药、停止溶气水进入,进入静止气浮分离时间,当微气泡粘附悬浮物上升到气浮分离池最高液面处时,开启刮渣机,由刮渣板进行旋转刮渣,浮渣由排渣口排出,刮渣完毕后开启出水阀,气浮分离后的清水由底部出水孔和穿孔出水管集合排出,进入产水池。气浮分离池中的水排放完毕后,再开启原水泵进入下一个周期。A new batch-type dissolved air flotation solid-liquid separation device described in this patent, the raw water in the raw water pool to be treated is lifted by the raw water pump, the coagulant enters the pipeline mixer through the dosing valve, and flows through the pipeline reactor. The dissolved air water enters the pipeline reactor through the dissolved air water inlet valve, and the reacted water and dissolved air water enter the air flotation separation tank together. When the water level rises to the highest level, the liquid level sensor senses it and is controlled by the main control box. Stop water intake, stop dosing, stop entering dissolved air water, and enter the static air flotation separation time. When the microbubble adhered suspended matter rises to the highest liquid level of the air flotation separation tank, start the slag scraper, and the slag scraper will carry out the process. The scum is scraped by rotation, and the scum is discharged from the slag discharge port. After the scum is scraped, the water outlet valve is opened, and the clean water after air flotation separation is discharged from the bottom water outlet hole and the perforated water outlet pipe, and enters the water production tank. After the water in the air flotation separation tank is discharged, the raw water pump is turned on to enter the next cycle.

本专利所述的一种新型序批式溶气气浮固液分离装置,具有如下优点:A new sequence batch type dissolved air flotation solid-liquid separation device described in this patent has the following advantages:

1、气浮分离池独立设置,浮渣上升时,水流是上升或静止的,使气浮分离水力条件达到理想化,从而大大提高溶气气浮分离效率和效果;1. The air flotation separation tank is set independently. When the scum rises, the water flow is rising or static, so that the hydraulic conditions of the air flotation separation can be idealized, thereby greatly improving the efficiency and effect of the dissolved air flotation separation;

2、采用管式混合器,溶气水由管式反应器的中部进入,接触区为管式,原水、药剂和溶气水在管式反应器中反应接触,创造了微气泡与混凝絮体的共聚环境,为共聚气浮创造了条件,分离更充分,且不易堵塞。2. A tubular mixer is adopted, and the dissolved air water enters from the middle of the tubular reactor, and the contact area is tubular, and the raw water, medicament and dissolved air water react and contact in the tubular reactor, creating microbubbles and coagulation flocculation The copolymerization environment of the body creates conditions for the copolymerization air flotation, the separation is more sufficient, and it is not easy to block.

附图说明Description of drawings

图1为本实用新型的一种新型序批式溶气气浮固液分离装置的结构示意图。Fig. 1 is a structural schematic diagram of a new sequencing batch type dissolved air flotation solid-liquid separation device of the present invention.

具体实施方式detailed description

如图1所示,本实用新型的一种新型序批式溶气气浮固液分离装置,包括管式反应器5,所述管式反应器5的前端安装有管式混合器4,所述管式混合器4的前端连接有一条进水管13的一端,所述进水管13的另一端通过三通分别连接有一个加药阀3和一个进水阀2,所述进水阀2的另一端连接有一个原水泵1。As shown in Fig. 1, a kind of novel sequential batch type dissolved air flotation solid-liquid separation device of the present utility model comprises tubular reactor 5, and the front end of described tubular reactor 5 is equipped with tubular mixer 4, so The front end of the tubular mixer 4 is connected with one end of a water inlet pipe 13, and the other end of the water inlet pipe 13 is respectively connected with a dosing valve 3 and a water inlet valve 2 through a tee, and the water inlet valve 2 The other end is connected with a raw water pump 1 .

所述管式反应器5的后端连接一个气浮分离池7的底部进水口16。The rear end of the tubular reactor 5 is connected to a bottom water inlet 16 of an air flotation separation tank 7 .

所述气浮分离池7的内部下半部分设置有多条表面打有多排出水孔8的穿孔出水管14,所述穿孔出水管14的一端封闭,另一端连接设置于气浮分离池7外部的出水阀9;所述气浮分离池7的顶部左侧设置有一个液位传感器11,所述气浮分离池7的顶部右侧设置有一个刮渣机10,所述刮渣机10的底部设置有底部略低于最高液面17的刮渣板18;所述气浮分离池7的右侧壁上、与最高液面17持平的位置开有一个排渣口15。The inner lower half of the air flotation separation tank 7 is provided with a plurality of perforated water outlet pipes 14 with multiple discharge holes 8 on the surface. One end of the perforated water outlet pipe 14 is closed, and the other end is connected to the air flotation separation tank 7. External water outlet valve 9; a liquid level sensor 11 is provided on the top left side of the air flotation separation tank 7, and a slag scraper 10 is provided on the top right side of the air flotation separation tank 7, and the slag scraper 10 The bottom of the tank is provided with a slag scraper 18 whose bottom is slightly lower than the highest liquid level 17; on the right side wall of the air flotation separation tank 7, a slag outlet 15 is opened at a position equal to the highest liquid level 17.

所述原水泵1、进水阀2、加药阀3、液位传感器11、刮渣机10、出水阀9、进溶气水阀6均同时连接总控箱12。The raw water pump 1, water inlet valve 2, dosing valve 3, liquid level sensor 11, slag scraper 10, water outlet valve 9, and dissolved air inlet valve 6 are all connected to the master control box 12 at the same time.

本专利所述的一种新型序批式溶气气浮固液分离装置,待处理的原水池的原水A由原水泵1提升,混凝剂E由加药阀3进入管道混合器4,流经管道反应器5,溶气水C通过进溶气水阀6进入管道反应器5,反应后的水与溶气水共同进入气浮分离池7,当水位上升到最高液位17时,液位传感器11感应到,受总控制箱12控制,停止进水、停止加药、停止溶气水进入,进入静止气浮分离时间,当微气泡粘附悬浮物上升到气浮分离池7最高液面处时,开启刮渣机10,由刮渣板18进行旋转刮渣,浮渣由排渣口15排出,刮渣完毕后开启出水阀9,气浮分离后的清水由底部出水孔8和穿孔出水管14集合排出,进入产水池。气浮分离池7中的水排放完毕后,再开启原水泵1进入下一个周期。A new batch-type dissolved air flotation solid-liquid separation device described in this patent, the raw water A of the raw water pool to be treated is lifted by the raw water pump 1, and the coagulant E enters the pipeline mixer 4 through the dosing valve 3, and flows Through the pipeline reactor 5, the dissolved air water C enters the pipeline reactor 5 through the dissolved air water inlet valve 6, and the reacted water and the dissolved air water enter the air flotation separation tank 7 together. When the water level rises to the highest liquid level 17, the liquid The level sensor 11 senses, and is controlled by the master control box 12, stops water intake, stops dosing, stops dissolved air water to enter, and enters the static air flotation separation time. When the surface is on the surface, open the slag scraper 10, and the scum scraper 18 rotates to scrape the scum. The scum is discharged from the slag discharge port 15. After the scum is scraped, the water outlet valve 9 is opened. The perforated water outlet pipe 14 is collectively discharged and enters the water production tank. After the water in the air flotation separation tank 7 is discharged, the raw water pump 1 is turned on to enter the next cycle.

上面所述的实施例仅仅是对本实用新型的优选实施方式进行描述,并非对本实用新型的范围进行限定,在不脱离本实用新型设计精神前提下,本领域普通工程技术人员对本实用新型技术方案做出的各种变形和改进,均应落入本实用新型的权利要求书确定的保护范围内。The above-mentioned embodiments are only descriptions of preferred implementations of the present utility model, and are not intended to limit the scope of the present utility model. The various deformations and improvements made should fall within the protection scope determined by the claims of the present utility model.

Claims (2)

1.一种新型序批式溶气气浮固液分离装置,其特征在于,包括管式反应器,所述管式反应器的前端安装有管式混合器,所述管式混合器的前端连接有一条进水管的一端,所述进水管的另一端通过三通分别连接有一个加药阀和一个进水阀,所述进水阀的另一端连接有一个原水泵;所述管式反应器的后端连接一个气浮分离池的底部进水口;所述气浮分离池的内部下半部分设置有多条表面打有多排出水孔的穿孔出水管,所述穿孔出水管的一端封闭,另一端连接设置于气浮分离池外部的出水阀;所述气浮分离池的顶部左侧设置有一个液位传感器,所述气浮分离池的顶部右侧设置有一个刮渣机,所述刮渣机的底部设置有底部略低于最高液面的刮渣板;所述气浮分离池的右侧壁上、与最高液面持平的位置开有一个排渣口。1. A novel sequence batch type dissolved air flotation solid-liquid separation device is characterized in that it comprises a tubular reactor, the front end of the tubular reactor is equipped with a tubular mixer, and the front end of the tubular mixer One end of a water inlet pipe is connected, and the other end of the water inlet pipe is respectively connected with a dosing valve and a water inlet valve through a tee, and the other end of the water inlet valve is connected with a raw water pump; the tubular reaction The rear end of the device is connected to the bottom water inlet of an air flotation separation tank; the inner lower half of the air flotation separation tank is provided with a plurality of perforated water outlet pipes with multiple discharge holes on the surface, and one end of the perforated water outlet pipe is closed , the other end is connected to the water outlet valve arranged outside the air flotation separation tank; a liquid level sensor is provided on the left side of the top of the air flotation separation tank, and a slag scraper is provided on the top right side of the air flotation separation tank, so The bottom of the slag scraper is provided with a slag scraper whose bottom is slightly lower than the highest liquid level; a slag outlet is opened on the right side wall of the air flotation separation tank at a position equal to the highest liquid level. 2.根据权利要求1所述的一种新型序批式溶气气浮固液分离装置,其特征在于,所述原水泵、进水阀、加药阀、液位传感器、刮渣机、出水阀、进溶气水阀均同时连接总控箱。2. A new sequence batch type dissolved air flotation solid-liquid separation device according to claim 1, characterized in that the raw water pump, water inlet valve, dosing valve, liquid level sensor, slag scraper, water outlet The valve and the dissolved air water valve are connected to the master control box at the same time.
CN201720570001.9U 2017-05-22 2017-05-22 A kind of new batch-type air-dissolving air-float equipment for separating liquid from solid Expired - Fee Related CN207031014U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107176643A (en) * 2017-05-22 2017-09-19 河北工程大学 A kind of new batch-type air-dissolving air-float solid-liquid separation system
CN113354022A (en) * 2021-05-26 2021-09-07 江西台标环保有限公司 Sewage air-flotation treatment device based on liquid level buoyancy change intermittent scraping and deslagging

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107176643A (en) * 2017-05-22 2017-09-19 河北工程大学 A kind of new batch-type air-dissolving air-float solid-liquid separation system
CN113354022A (en) * 2021-05-26 2021-09-07 江西台标环保有限公司 Sewage air-flotation treatment device based on liquid level buoyancy change intermittent scraping and deslagging

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