CN209098368U - A high-concentration sewage treatment air flotation equipment - Google Patents

A high-concentration sewage treatment air flotation equipment Download PDF

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CN209098368U
CN209098368U CN201821529324.4U CN201821529324U CN209098368U CN 209098368 U CN209098368 U CN 209098368U CN 201821529324 U CN201821529324 U CN 201821529324U CN 209098368 U CN209098368 U CN 209098368U
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water
contact chamber
pond body
air flotation
concentration sewage
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戴文强
赵洪启
樊洁
徐军
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WUXI HI-TECH ENVIRONMENTAL PROTECTION EQUIPMENT TECHNOLOGY Co Ltd
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WUXI HI-TECH ENVIRONMENTAL PROTECTION EQUIPMENT TECHNOLOGY Co Ltd
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Abstract

The utility model relates to a kind of high-concentration sewages to handle airfloat equipment, including pond body, interconnected contact chamber and separation chamber are equipped in pond body, further include being connected to contact chamber for launching the adding of agent mouth of flocculant or coagulant, is additionally provided with the release for discharging dissolved air water and the agitating device for stirring liquid in contact chamber.The high-concentration sewage processing airfloat equipment wadding body of the utility model is not easy, sewage treating efficiency is high.

Description

一种高浓度污水处理气浮设备A high-concentration sewage treatment air flotation equipment

技术领域technical field

本实用新型涉及一种用于污水处理的气浮设备,尤其涉及一种高浓度污水处理气浮设备。The utility model relates to an air flotation device for sewage treatment, in particular to an air flotation device for high-concentration sewage treatment.

背景技术Background technique

在给水排水处理工艺程序中,固、液分离技术及其设备是关键项目之一。常规气浮主要应用于分离密度与水相近的悬浮物质,且悬浮物沉降性能较差的废水处理中。In the water supply and drainage treatment process, the solid and liquid separation technology and its equipment are one of the key items. Conventional air flotation is mainly used for the separation of suspended matter with a density similar to that of water, and the treatment of wastewater with poor sedimentation performance of the suspended matter.

常规气浮主要工作原理是将空气与水在一定的压力和条件下,使气体极大限度地溶入水中,然后把所形成的压力溶气水通过布置在接触室内的溶气释放器释压,急速产生大量的微气泡。这些微气泡布满接触室形成类似牛奶一样的“白水”。污水在絮凝剂和混凝剂的化学作用下产生“絮凝体”俗称“矾花”。“絮凝体”随着水流流入气浮池体内部混合接触室,在这里和大量的微气泡相互粘接成“沾气絮体”(絮体外部表面沾满气泡),其视密度小于水,“沾气絮体”很快升至水面,悬浮物在液面结聚成浮渣,把浮渣进行刮集即达到了固液分离的目的。常规负荷气浮其表面负荷可以做到2~7M3/M2/h。所以常规气浮设计在100 吨/小时处理量时外形尺寸达到10000×3800,其已经达到运输的极限,无法再做大,根据设计规范其分离区内长宽比达到1:2甚至达到1:3在分离区的尾端溶气水很少甚至没有。所以出水处理效果也差。常规气浮效率低,出水效果差,只能做到100吨/小时,超过该值的气浮设备由于尺寸过大就不能运输了。常规气浮处理能力上进水悬浮物密度在1000毫克/L以内,进水中污染物浓度超过这个值就不能达到100吨/小时的处理量,只能减少到60~70吨/小时。The main working principle of conventional air flotation is to dissolve air and water into the water to the greatest extent under certain pressure and conditions, and then release the pressure of the formed pressure-dissolved water through the dissolved air releaser arranged in the contact chamber. , a large number of microbubbles are rapidly generated. These microbubbles fill the contact chamber to form "white water" similar to milk. Sewage produces "flocs" under the chemical action of flocculants and coagulants, commonly known as "alum flowers". "Flocs" flow into the mixing and contact chamber inside the air flotation tank with the water flow, where they bond with a large number of micro-bubbles to form "air-stained flocs" (the outer surface of the flocs is covered with air bubbles), and its apparent density is lower than that of water, " The air-dipped flocs quickly rise to the water surface, and the suspended matter condenses on the liquid surface to form scum, and the purpose of solid-liquid separation is achieved by scraping the scum. The surface load of conventional load air flotation can be 2~7M 3 /M 2 /h. Therefore, the conventional air flotation design has an external dimension of 10000×3800 when the processing capacity is 100 tons/hour, which has reached the limit of transportation and cannot be enlarged any more. According to the design specification, the aspect ratio in the separation zone reaches 1:2 or even 1: 3 There is little or no dissolved gas and water at the end of the separation zone. Therefore, the effluent treatment effect is also poor. Conventional air flotation has low efficiency and poor water discharge effect, and can only achieve 100 tons/hour. Air flotation equipment exceeding this value cannot be transported due to its large size. In terms of conventional air flotation treatment capacity, the density of suspended solids in the influent water is within 1000 mg/L. If the concentration of pollutants in the influent water exceeds this value, the treatment capacity cannot reach 100 tons/hour, and can only be reduced to 60-70 tons/hour.

目前工业废水市场上,流量超过300吨/小时,进水悬浮物超过3000毫克/L 的废水很多,常规气浮需要配置4台100吨/小时的气浮,从而增加了污水处理设备的成本及占地面积,因此,需要研发一种处理流量在300吨/小时以上,进水悬浮物超过3000毫克/L的高效溶气气浮并且体积在11000×3800可以运输的气浮,来替代常规气浮。At present, in the industrial wastewater market, there are many wastewaters with a flow rate of more than 300 tons/hour and influent suspended solids exceeding 3000 mg/L. Conventional air flotation needs to be equipped with 4 sets of 100 tons/hour air floats, which increases the cost and cost of sewage treatment equipment. Therefore, it is necessary to develop a high-efficiency dissolved air flotation with a processing flow rate of more than 300 tons/hour and a suspended solids of more than 3000 mg/L in the influent and a volume of 11000×3800 that can be transported to replace conventional air flotation. float.

而目前,影响常规气浮处理能力的因素包括絮凝剂和混凝剂的投加方式,常规负荷气浮其工作时污水在气浮池体外部的混合反应区完成化学反应,反应产物也就是“絮凝体”通过管道等结构件输送到接触室内,在接触室内“絮凝体”和微小气泡相互作用粘接在一起形成“沾气絮体”。这个过程中微小气泡是粘接在“絮凝体”的身体外部。粘接的气泡数量和牢靠度由水质和药剂的成分决定。所以不同水质会有不同效果。因为“絮凝体”颗粒大小区别较大,颗粒上浮速度快慢相差很大,因此“沾气絮体”的表观密度变化很大。有的很快上浮,有的很慢。另外在分离区内水流扰动会让“沾气絮体”外部的气泡重新脱落,造成絮体在水体中随着水流流出。使出水变差,达不到业主的处理要求。At present, the factors that affect the treatment capacity of conventional air flotation include the dosing method of flocculants and coagulants. When the conventional load air flotation works, the sewage completes the chemical reaction in the mixing reaction zone outside the air flotation tank, and the reaction product is "flocculation". The "flocs" are transported to the contact chamber through structural parts such as pipes, and the "flocs" and tiny air bubbles interact and bond together in the contact chamber to form "air-stained flocs". During this process, tiny air bubbles are adhered to the outside of the body of the "floc". The number of air bubbles and the firmness of the bonding are determined by the water quality and the composition of the agent. So different water quality will have different effects. Because the particle size of "flocs" is very different, the speed of particles floating is very different, so the apparent density of "air-dipped flocs" varies greatly. Some rise quickly, some very slowly. In addition, the water flow disturbance in the separation zone will make the air bubbles outside the "air-dipped flocs" fall off again, causing the flocs to flow out with the water flow in the water body. Make the effluent worse and fail to meet the owner's treatment requirements.

有鉴于上述的缺陷,本发明人,积极加以研究创新,以期创设一种新型结构的高浓度污水处理气浮设备,使其更具有产业上的利用价值。In view of the above-mentioned defects, the inventors of the present invention have actively carried out research and innovation, in order to create a new type of high-concentration sewage treatment air flotation equipment, which has more industrial value.

实用新型内容Utility model content

为解决上述技术问题,本实用新型的目的是提供一种絮体不易下沉、污水处理效率高的高浓度污水处理气浮设备。In order to solve the above-mentioned technical problems, the purpose of this utility model is to provide a high-concentration sewage treatment air flotation device with which the flocs are not easy to sink and the sewage treatment efficiency is high.

本实用新型的高浓度污水处理气浮设备,包括池体,池体内设有相互连通的接触室和分离室,还包括与接触室连通的用于投放絮凝剂或混凝剂的药剂投加口,接触室内还设有用于释放溶气水的释放器以及用于搅拌液体的搅拌装置。The high-concentration sewage treatment air flotation device of the utility model comprises a pool body, wherein the pool body is provided with a contact chamber and a separation chamber which are communicated with each other, and also includes a medicament feeding port which is communicated with the contact chamber and is used for feeding flocculant or coagulant. , the contact chamber is also provided with a releaser for releasing dissolved gas water and a stirring device for stirring liquid.

作为优选,本实用新型的高浓度污水处理气浮设备,搅拌装置包括设于池体上的驱动电机、与驱动电机输出轴连接的连接轴、设于连接轴并位于接触室内的搅拌桨叶。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, the stirring device includes a driving motor arranged on the tank body, a connecting shaft connected to the output shaft of the driving motor, and a stirring blade arranged on the connecting shaft and located in the contact chamber.

作为优选,本实用新型的高浓度污水处理气浮设备,池体的一端设置有污水池,池体的中部设有与污水池连通的污水进水管,池体的两端对称地设有接触室及分离室,污水进水管通过污水配水管与接触室连通,接触室的底部设置有配水板,配水板的表面设有多个配水孔,污水配水管的出水端位于配水板的下方。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, one end of the pool body is provided with a sewage pool, the middle of the pool body is provided with a sewage water inlet pipe that communicates with the sewage pool, and the two ends of the pool body are symmetrically provided with contact chambers And the separation chamber, the sewage water inlet pipe is connected with the contact chamber through the sewage water distribution pipe, the bottom of the contact chamber is provided with a water distribution plate, the surface of the water distribution plate is provided with a plurality of water distribution holes, and the outlet end of the sewage water distribution pipe is located below the water distribution plate.

作为优选,本实用新型的高浓度污水处理气浮设备,分离室内也设置有释放器。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, a releaser is also arranged in the separation chamber.

作为优选,本实用新型的高浓度污水处理气浮设备,池体的一端设有气泡发生器,气泡发生器的输出端通过管道与释放器连通。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, one end of the pool body is provided with a bubble generator, and the output end of the bubble generator is communicated with the releaser through a pipeline.

作为优选,本实用新型的高浓度污水处理气浮设备,分离室的底部设有清水收集装置,清水收集装置包括总管和对称设于总管两端的收集组件,收集组件包括一端与总管连通、另一端与连接管连通的主管,连接管的上下两端分别对称地设有位于连接管左右两侧的两根支管,支管上设有收水孔。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, a clean water collection device is provided at the bottom of the separation chamber. The clean water collection device includes a main pipe and a collection assembly symmetrically arranged at both ends of the main pipe. The collection assembly includes one end that communicates with the main pipe and the other end The main pipe communicated with the connecting pipe, the upper and lower ends of the connecting pipe are respectively symmetrically provided with two branch pipes located on the left and right sides of the connecting pipe, and the branch pipes are provided with water collecting holes.

借由上述方案,本实用新型至少具有以下优点:本实用新型的高浓度污水处理气浮设备,在接触室区域内布满由释放器释放的小于微米级的小气泡。因为气泡总数非常大,表观像一杯牛奶倒入这个区域内。混凝剂和污水在搅拌装置的作用下发生化学反应,产生“絮凝体”。“絮凝体”由小到大的生长过程中会把周边的微小气泡逐步“包裹”在“絮凝体”的内部。形成一个体内夹气的絮凝体。简称“夹气絮体”。“夹气絮体”颗粒粒径大于常规气浮,而且其身体内部含有气泡,其整体表观密度远远小于水,几乎几十秒内就可以升至液面,悬浮物在液面结聚成浮渣,把浮渣进行刮集即达到了固液分离的目的。With the above solution, the present invention has at least the following advantages: the high-concentration sewage treatment air flotation equipment of the present invention is filled with small bubbles smaller than micron level released by the releaser in the contact chamber area. Because the total number of bubbles is very large, it appears to be poured into this area like a glass of milk. The coagulant and sewage react chemically under the action of the stirring device to produce "flocs". During the growth process of "flocs" from small to large, the surrounding tiny air bubbles will gradually "envelope" inside the "flocs". Forms a floc with air in the body. Referred to as "air-filled flocs". The particle size of "air-inclusion flocs" is larger than that of conventional air flotation, and its body contains air bubbles, and its overall apparent density is much smaller than that of water. The purpose of solid-liquid separation is achieved by scraping the scum into scum.

综上,本实用新型的高浓度污水处理气浮设备絮体不易下沉、污水处理效率高。In conclusion, the flocs of the high-concentration sewage treatment air flotation equipment of the present invention are not easy to sink, and the sewage treatment efficiency is high.

上述说明仅是本实用新型技术方案的概述,为了能够更清楚了解本实用新型的技术手段,并可依照说明书的内容予以实施,以下以本实用新型的较佳实施例并配合附图详细说明如后。The above description is only an overview of the technical solution of the present utility model. In order to understand the technical means of the present utility model more clearly, and to implement it according to the contents of the specification, the following is a detailed description of the preferred embodiment of the present utility model and the accompanying drawings as follows: back.

附图说明Description of drawings

图1是本实用新型的高浓度污水处理气浮设备的结构示意图;Fig. 1 is the structural representation of the high-concentration sewage treatment air flotation equipment of the present invention;

图2是高浓度污水处理气浮设备的俯视示意图,其中刮渣机等部件未示出;Figure 2 is a schematic top view of a high-concentration sewage treatment air flotation device, wherein parts such as a slag scraper are not shown;

图3是污水配水管、配水板等结构在池体中的结构示意图;Figure 3 is a schematic structural diagram of the sewage water distribution pipe, water distribution plate and other structures in the tank body;

图4是污水配水管、配水板等结构以及污水池的俯视示意图;Fig. 4 is the top view schematic diagram of sewage water distribution pipe, water distribution plate and other structures and sewage pool;

图5是清水收集装置的结构示意图;Fig. 5 is the structural representation of clear water collecting device;

图6是图1中A部的局部放大图。FIG. 6 is a partial enlarged view of part A in FIG. 1 .

图中,1:池体;2:接触室;3:分离室;4:药剂投加口;5:释放器;6:驱动电机;7:连接轴;8:搅拌桨叶;9:污水池;10:污水进水管;11:污水配水管;12:配水板;13:配水孔;14:气泡发生器;15:总管;16:收集组件;17:主管;18:支管;19:收水孔;20:连接管。In the figure, 1: tank body; 2: contact chamber; 3: separation chamber; 4: chemical injection port; 5: releaser; 6: drive motor; 7: connecting shaft; 8: stirring blade; 9: sewage pool ;10: Sewage inlet pipe; 11: Sewage water distribution pipe; 12: Water distribution plate; 13: Water distribution hole; 14: Bubble generator; 15: Main pipe; 16: Collection component; 17: Main pipe; 18: Branch pipe; hole; 20: connecting pipe.

具体实施方式Detailed ways

下面结合附图和实施例,对本实用新型的具体实施方式作进一步详细描述。以下实施例用于说明本实用新型,但不用来限制本实用新型的范围。The specific embodiments of the present utility model will be described in further detail below with reference to the accompanying drawings and embodiments. The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention.

参见图1至图6,本实用新型一较佳实施例的一种高浓度污水处理气浮设备,包括池体1,池体内设有相互连通的接触室2和分离室3,还包括与接触室连通的用于投放絮凝剂或混凝剂的药剂投加口4,接触室内还设有用于释放溶气水的释放器5以及用于搅拌液体的搅拌装置。Referring to FIGS. 1 to 6 , a high-concentration sewage treatment air flotation device according to a preferred embodiment of the present invention includes a pool body 1, and the pool body is provided with a contact chamber 2 and a separation chamber 3 that communicate with each other, and also includes a contact chamber 2 and a separation chamber 3 that communicate with each other. The chamber is connected to a medicament feeding port 4 for feeding flocculant or coagulant, and the contact chamber is also provided with a releaser 5 for releasing dissolved gas water and a stirring device for stirring liquid.

具体地,药剂投加口可以是顶端伸出接触室液面的管道的管口,管道的底端位于接触室的底部。Specifically, the medicament feeding port may be a pipe port of a pipe whose top end protrudes from the liquid level of the contact chamber, and the bottom end of the pipe is located at the bottom of the contact chamber.

高浓度污水处理气浮设备在接触室区域内布满由释放器释放的小于微米级的小气泡。因为气泡总数非常大,表观像一杯牛奶倒入这个区域内。混凝剂和污水在搅拌装置的作用下发生化学反应,产生“絮凝体”。“絮凝体”由小到大的生长过程中会把周边的微小气泡逐步“包裹”在“絮凝体”的内部。形成一个体内夹气的絮凝体。简称“夹气絮体”。“夹气絮体”颗粒粒径大于常规气浮,而且其身体内部含有气泡,其整体表观密度远远小于水,几乎几十秒内就可以升至液面,悬浮物在液面结聚成浮渣,把浮渣进行刮集即达到了固液分离的目的。The air flotation equipment for high-concentration sewage treatment is filled with small air bubbles smaller than micron level released by the releaser in the contact chamber area. Because the total number of bubbles is very large, it appears to be poured into this area like a glass of milk. The coagulant and sewage react chemically under the action of the stirring device to produce "flocs". During the growth process of "flocs" from small to large, the surrounding tiny air bubbles will gradually "envelope" inside the "flocs". Forms a floc with air in the body. Referred to as "air-filled flocs". The particle size of "air-inclusion flocs" is larger than that of conventional air flotation, and its body contains air bubbles, and its overall apparent density is much smaller than that of water. The purpose of solid-liquid separation is achieved by scraping the scum into scum.

高浓度污水处理气浮设备在混合接触区内产生“夹气絮体”。微小气泡是“包裹”在“絮凝体”的内部。“夹气絮体”内部“包裹”的气泡数量远多于常规负荷气浮产生的“沾气絮体”。“夹气絮体”的牢靠度也好于常规气浮产生的“沾气絮体”。“夹气絮体”的表观密度也远远小于“沾气絮体”。二者在气浮分离区中上升速度差别非常大,所以高浓度污水处理气浮设备气浮效率很高,一台可以当四台常规气浮用。The high-concentration sewage treatment air flotation equipment produces "air-inclusion flocs" in the mixed contact area. The tiny air bubbles are "wrapped" inside the "floc". The number of bubbles "wrapped" inside the "air-entrained flocs" is much more than the "air-impregnated flocs" produced by conventional load flotation. The reliability of "air-entrained flocs" is also better than that of "air-impregnated flocs" produced by conventional air flotation. The apparent density of "air-entrained flocs" is also much smaller than that of "air-impregnated flocs". The difference in the rising speed of the two in the air flotation separation area is very large, so the air flotation efficiency of the high-concentration sewage treatment air flotation equipment is very high, and one can be used as four conventional air flotations.

基于上述描述,高浓度污水处理气浮设备的表面负荷可以达到 12~20M3/M2/h。常规溶气气浮的表面负荷只能做到3~7M3/M2/h。两者相差3~5 倍。占地面积上高浓度污水处理气浮设备是常规负荷气浮的1/3~1/5。Based on the above description, the surface load of air flotation equipment for high-concentration sewage treatment can reach 12-20M3/M2/h. The surface load of conventional dissolved air flotation can only achieve 3 ~ 7M3/M2/h. The difference between the two is 3 to 5 times. The high-concentration sewage treatment air flotation equipment on the floor area is 1/3 to 1/5 of the conventional load air flotation.

作为优选,本实用新型的高浓度污水处理气浮设备,搅拌装置包括设于池体上的驱动电机6、与驱动电机输出轴连接的连接轴7、设于连接轴并位于接触室内的搅拌桨叶8。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, the stirring device includes a driving motor 6 arranged on the tank body, a connecting shaft 7 connected to the output shaft of the driving motor, and a stirring paddle arranged on the connecting shaft and located in the contact chamber. Leaf 8.

作为优选,本实用新型的高浓度污水处理气浮设备,池体的一端设置有污水池9,池体的中部设有与污水池连通的污水进水管10,池体的两端对称地设有接触室及分离室,污水进水管通过污水配水管11与接触室连通,接触室的底部设置有配水板12,配水板的表面设有多个配水孔13,污水配水管的出水端位于配水板的下方。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, one end of the pool body is provided with a sewage pool 9, the middle part of the pool body is provided with a sewage water inlet pipe 10 that communicates with the sewage pool, and both ends of the pool body are symmetrically provided with The contact chamber and the separation chamber, the sewage water inlet pipe is communicated with the contact chamber through the sewage water distribution pipe 11, the bottom of the contact chamber is provided with a water distribution plate 12, the surface of the water distribution plate is provided with a plurality of water distribution holes 13, and the outlet end of the sewage water distribution pipe is located on the water distribution plate below.

常规气浮池体形状一般为长方形,长宽比多为3:1有的甚至到5:1。进水方式一般为短边进水,水流沿着长边行走至对面的短边出水。水流沿着长边方向流到池体端部。这种池体结构形式在刮渣过程中,由于路程过长,沿途掉落至池底的浮渣过多,严重时会影响出水水质。高浓度污水处理气浮设备将进水方式更改为池体中部进水,通过管路一分为二,进入两端的接触室。这项改进相当于将常规溶气气浮从中间一分为二。将常规溶气气浮分离区一分为二,污水和絮体在分离区内的流动距离缩短一半。The shape of the conventional air flotation tank is generally rectangular, and the aspect ratio is mostly 3:1, and some even reach 5:1. The water inlet method is generally the short side of the water, and the water flows along the long side to the opposite short side. The water flow flows to the end of the tank body along the long side direction. In the process of scraping the slag with this type of pool structure, due to the long distance, too much scum falls to the bottom of the pool along the way, which will seriously affect the quality of the effluent. The high-concentration sewage treatment air flotation equipment changes the water inlet mode to the water inlet in the middle of the pool body, which is divided into two parts through the pipeline and enters the contact chambers at both ends. This improvement is equivalent to splitting the conventional dissolved air flotation in two from the middle. The conventional dissolved air flotation separation zone is divided into two parts, and the flow distance of sewage and flocs in the separation zone is shortened by half.

配水板根据水头大小配有孔径大小不一配水孔,目的让接触室内水流能够均匀上升。The water distribution plate is equipped with water distribution holes of different sizes according to the size of the water head, so that the water flow in the contact room can rise evenly.

作为优选,本实用新型的高浓度污水处理气浮设备,分离室内也设置有释放器。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, a releaser is also arranged in the separation chamber.

作为优选,本实用新型的高浓度污水处理气浮设备,池体的一端设有气泡发生器14,气泡发生器的输出端通过管道与释放器连通。Preferably, in the high-concentration sewage treatment air flotation device of the present invention, a bubble generator 14 is provided at one end of the pool body, and the output end of the bubble generator is communicated with the releaser through a pipeline.

常规气浮池体形状一般为长方形,长宽比多为3:1有的甚至到5:1。进水方式一般为短边进水,水流沿着长边行走至对面的短边出水。水流沿着长边方向流到池体端部。这种池体结构形式在刮渣过程中,由于路程过长,沿途掉落至池底的浮渣过多,严重时会影响出水水质。高浓度污水处理气浮设备将进水方式更改为池体中部进水,通过管路一分为二,进入两端的接触室。这项改进相当于将常规溶气气浮从中间一分为二。将常规溶气气浮分离区一分为二,污水和絮体在分离区内的流动距离缩短一半。The shape of the conventional air flotation tank is generally rectangular, and the aspect ratio is mostly 3:1, and some even reach 5:1. The water inlet method is generally the short side of the water, and the water flows along the long side to the opposite short side. The water flow flows to the end of the tank body along the long side direction. In the process of scraping the slag with this type of pool structure, due to the long distance, too much scum falls to the bottom of the pool along the way, which will seriously affect the quality of the effluent. The high-concentration sewage treatment air flotation equipment changes the water inlet mode to the water inlet in the middle of the pool body, which is divided into two parts through the pipeline and enters the contact chambers at both ends. This improvement is equivalent to splitting the conventional dissolved air flotation in two from the middle. The conventional dissolved air flotation separation zone is divided into two parts, and the flow distance of sewage and flocs in the separation zone is shortened by half.

配水板根据水头大小配有孔径大小不一配水孔,目的让接触室内水流能够均匀上升。The water distribution plate is equipped with water distribution holes of different sizes according to the size of the water head, so that the water flow in the contact room can rise evenly.

作为优选,本实用新型的高浓度污水处理气浮设备,分离室的底部设有清水收集装置,清水收集装置包括总管15和对称设于总管两端的收集组件16,收集组件包括一端与总管连通、另一端与连接管20连通的主管17,连接管的上下两端分别对称地设有位于连接管左右两侧的两根支管18,支管上设有收水孔19。Preferably, in the high-concentration sewage treatment air flotation equipment of the present invention, a clean water collecting device is provided at the bottom of the separation chamber. The clean water collecting device includes a main pipe 15 and a collection assembly 16 symmetrically arranged at both ends of the main pipe. The collecting assembly includes one end that communicates with the main pipe, The other end of the main pipe 17 communicates with the connecting pipe 20. The upper and lower ends of the connecting pipe are symmetrically provided with two branch pipes 18 located on the left and right sides of the connecting pipe respectively, and the branch pipes are provided with water collecting holes 19.

高浓度污水处理气浮设备采用的清水收集装置整体的长度只有常规气浮的一半,所以极大避免了孔洞压力损失带来的水量不均匀性,收集上来的清水采用丁字管输送,这样做的好处是提高整个收水系统的压力水头,可以极大提高整个收水系统收水的均匀性,让整个分离区全面积上都能够均匀收集清水,不会发生短路,如果短路会造成局部水力负荷过大,影响“夹气絮体”的上浮,甚至直接将絮体带出,严重时影响出水效果。The overall length of the clean water collection device used in the high-concentration sewage treatment air flotation equipment is only half of the conventional air flotation, so it greatly avoids the unevenness of the water volume caused by the pressure loss of the holes. The collected clean water is transported by a T-shaped pipe. The advantage is to increase the pressure head of the entire water collection system, which can greatly improve the uniformity of water collection in the entire water collection system, so that the entire separation area can collect clean water evenly over the entire area, without short-circuiting, which will cause local hydraulic loads. If it is too large, it will affect the floating of "air-entrained flocs", and even directly bring the flocs out, which will affect the water effluent effect in serious cases.

对于本领域技术人员而言,显然本实用新型不限于上述示范性实施例的细节,而且在不背离本实用新型的精神或基本特征的情况下,本领域技术人员能够以其他的具体形式实现本实用新型。因此,无论从哪一点来看,均应将实施例看作是示范性的,而且是非限制性的,本实用新型的保护范围由所附权利要求而不是上述说明限定。For those skilled in the art, it is obvious that the present invention is not limited to the details of the above-mentioned exemplary embodiments, and that those skilled in the art can implement the present invention in other specific forms without departing from the spirit or essential characteristics of the present invention. Utility model. Therefore, the embodiments should be regarded as exemplary and non-restrictive from any point of view, and the protection scope of the present invention is defined by the appended claims rather than the foregoing description.

此外,以上仅是本实用新型的优选实施方式,并不用于限制本实用新型,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型技术原理的前提下,还可以做出若干改进和变型,这些改进和变型也应视为本实用新型的保护范围。同时,应当理解,虽然本说明书按照实施方式加以描述,但并非每个实施方式仅包含一个独立的技术方案,说明书的这种叙述方式仅仅是为清楚起见,本领域技术人员应当将说明书作为一个整体,各实施例中的技术方案也可以经适当组合,形成本领域技术人员可以理解的其他实施方式。In addition, the above are only the preferred embodiments of the present invention and are not intended to limit the present invention. It should be pointed out that for those skilled in the art, without departing from the technical principles of the present invention, the Several improvements and modifications are made, and these improvements and modifications should also be regarded as the protection scope of the present invention. At the same time, it should be understood that although this specification is described in terms of embodiments, not each embodiment only includes an independent technical solution, and this description in the specification is only for the sake of clarity, and those skilled in the art should take the specification as a whole , the technical solutions in each embodiment can also be appropriately combined to form other implementations that can be understood by those skilled in the art.

Claims (6)

1. a kind of high-concentration sewage handles airfloat equipment, including pond body, interconnected contact chamber and separation chamber are equipped in pond body, It is characterized by also including being connected to contact chamber for launching the adding of agent mouth of flocculant or coagulant, gone back in contact chamber Equipped with the release for discharging dissolved air water and the agitating device for stirring liquid.
2. high-concentration sewage according to claim 1 handles airfloat equipment, it is characterised in that: the agitating device includes setting In in pond body driving motor, with driving motor output shaft connection connecting shaft, set on connecting shaft and be located at contact indoor stir Mix blade.
3. high-concentration sewage according to claim 1 handles airfloat equipment, it is characterised in that: one end of the pond body is arranged Have a cesspool, the middle part of pond body is equipped with the sewage water inlet pipe being connected to cesspool, the both ends of pond body be symmetrically equipped with contact chamber and Separation chamber, the sewage water inlet pipe are connected to by sewage sparge pipe with the contact chamber, and the bottom of contact chamber is provided with water dispensing board, The surface of the water dispensing board is equipped with multiple distributing holes, and the water outlet of the sewage sparge pipe is located at the lower section of the water dispensing board.
4. high-concentration sewage according to claim 1 handles airfloat equipment, it is characterised in that: be also provided in the separation chamber There is release.
5. high-concentration sewage according to claim 4 handles airfloat equipment, it is characterised in that: one end of pond body is equipped with bubble The output end of generator, the bubble generator is connected to by pipeline with the release.
6. high-concentration sewage according to claim 1 handles airfloat equipment, it is characterised in that: the bottom of the separation chamber is set There is clear water collection device, the clear water collection device includes general pipeline and the collection assembly for being symmetrically set in the both ends general pipeline, the collection Component includes the supervisor that one end is connected to general pipeline, the other end is connected to connecting tube, and the upper and lower ends of the connecting tube are respectively symmetrically Ground is equipped with two branch pipes being located at left and right sides of connecting tube, and the branch pipe, which is equipped with, receives water hole.
CN201821529324.4U 2018-09-18 2018-09-18 A high-concentration sewage treatment air flotation equipment Expired - Fee Related CN209098368U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108975562A (en) * 2018-09-18 2018-12-11 无锡海拓环保装备科技有限公司 A kind of high-concentration sewage processing airfloat equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108975562A (en) * 2018-09-18 2018-12-11 无锡海拓环保装备科技有限公司 A kind of high-concentration sewage processing airfloat equipment

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