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CN209835843U - Coagulation air flotation copolymerization quick separation device - Google Patents

Coagulation air flotation copolymerization quick separation device Download PDF

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Publication number
CN209835843U
CN209835843U CN201920616766.0U CN201920616766U CN209835843U CN 209835843 U CN209835843 U CN 209835843U CN 201920616766 U CN201920616766 U CN 201920616766U CN 209835843 U CN209835843 U CN 209835843U
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pipe
copolymerization
separation device
sewage
water
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费庆志
范文新
解欣宇
侯婷婷
许芝
肖经伦
邹之本
于岱卿
夏欣雨
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Dalian Jiaotong University
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Dalian Jiaotong University
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Abstract

本实用新型涉及环境工程技术领域,具体公开了一种混凝气浮共聚快速分离装置,包括污水池、进污水管、酸碱加入管、混凝剂加入管、污水泵、第一连接管、第一排水管、溶气泵、进气嘴、第二排水管、第一助凝剂加入管、共聚反应器箱体、第二助凝剂加入管、搅拌机、搅拌杆、导流管、分离装置箱体、隔板、沉泥收集管、浮渣收集槽、净水收集管、第三连接管、净水收集箱和出水管。本实用新型能够有效处理经混凝沉淀池处理后的污水中残留的杂质,处理操作简单,处理成本低,可有效去除污水中的悬浮颗粒、乳化油、纤维、重金属等杂质,环保无污染。

The utility model relates to the technical field of environmental engineering, and specifically discloses a coagulation air flotation copolymerization rapid separation device, comprising a sewage tank, a sewage inlet pipe, an acid-base adding pipe, a coagulant adding pipe, a sewage pump, a first connecting pipe, First drain pipe, dissolved air pump, air inlet nozzle, second drain pipe, first coagulant aid adding pipe, copolymerization reactor box, second coagulant aid adding pipe, mixer, stirring rod, diversion pipe, separation device A box body, a partition, a sediment collection pipe, a scum collection tank, a clean water collection pipe, a third connecting pipe, a clean water collection box and an outlet pipe. The utility model can effectively treat the residual impurities in the sewage treated by the coagulation sedimentation tank, the treatment operation is simple, the treatment cost is low, and the suspended particles, emulsified oil, fiber, heavy metal and other impurities in the sewage can be effectively removed, which is environmentally friendly and pollution-free.

Description

混凝气浮共聚快速分离装置Coagulation air flotation copolymerization quick separation device

技术领域technical field

本实用新型涉及环境工程技术领域,尤其涉及一种混凝气浮共聚快速分离装置。The utility model relates to the technical field of environmental engineering, in particular to a coagulation air flotation copolymerization quick separation device.

背景技术Background technique

随着我国人口不断增加,水资源遭到了严重破坏,我国面临着水资源枯竭的问题。水资源是人类赖以生存的保障,它是不可再生资源,它不仅仅影响人们的生产生活,更对我国的城市建设,提高我国的综合国力与国际竞争力有着重要的影响。由此可见,加强我国的城市污水处理工作刻不容缓。然而,近些年来,我国在城市化的过程中却造成了水资源污染的严重问题。城市污水排放量在不断增加,而我国的废水污染源主要有工业源、农业源、城镇生活源以及少部分的集中式污染设施排放源,其中,具有关资料显示,城镇生活污水排放量是增加我国污水排放量的主要原因。With the continuous increase of population in our country, water resources have been severely damaged, and our country is facing the problem of water resource depletion. Water resources are the guarantee for human survival. It is a non-renewable resource. It not only affects people's production and life, but also has an important impact on my country's urban construction and the improvement of my country's comprehensive national strength and international competitiveness. It can be seen that it is urgent to strengthen the urban sewage treatment work in our country. However, in recent years, the process of urbanization in my country has caused serious problems of water pollution. The amount of urban sewage discharge is increasing, and the sources of wastewater pollution in my country mainly include industrial sources, agricultural sources, urban living sources, and a small number of centralized pollution facility discharge sources. Among them, relevant data show that urban domestic sewage discharge is increasing in my country The main cause of sewage discharge.

另一方面,污水在污水处理厂的处理过程中,首先自流入粗格栅间,经粗格栅除去较大的漂浮杂物后,接着污水经细格栅除去细小漂浮物后,在旋流沉砂池中去除泥沙,沉积在沉砂池底部的泥沙经吸砂机排入污泥储存池内;经除砂后的污水进入如后端处理设施设备混凝沉淀池,混凝沉淀池主要去除污水中的悬浮固体颗粒物,而经混凝形成的絮体颗粒小、重量轻、沉淀性能差,这个污水处理带来了巨大的挑战。因此,实用新型一种污水处理方法来处理经混凝沉淀池处理后的污水中残留的杂质,对促进污水处理发展和保护水资源重复利用具有重要意义。On the other hand, during the treatment process of the sewage treatment plant, the sewage first flows into the coarse grid, and after the larger floating debris is removed through the coarse grid, then the sewage is removed through the fine grid to remove the fine floating debris, and then in the swirling flow. The sediment is removed in the grit chamber, and the sediment deposited at the bottom of the grit chamber is discharged into the sludge storage tank through the sand suction machine; the sewage after sand removal enters the coagulation sedimentation tank of the back-end treatment facilities and equipment, such as the coagulation sedimentation tank It mainly removes suspended solid particles in sewage, and the floc particles formed by coagulation are small, light in weight and poor in sedimentation performance. This sewage treatment has brought great challenges. Therefore, the utility model of a sewage treatment method to deal with the residual impurities in the sewage treated by the coagulation sedimentation tank is of great significance to promote the development of sewage treatment and protect the reuse of water resources.

实用新型内容Utility model content

本实用新型的目的是提供一种混凝气浮共聚快速分离装置,以有效处理经混凝沉淀池处理后的污水中残留的杂质。The purpose of the utility model is to provide a coagulation air flotation copolymerization rapid separation device to effectively treat the residual impurities in the sewage treated by the coagulation sedimentation tank.

为了解决上述技术问题,本实用新型提供了一种混凝气浮共聚快速分离装置,包括污水池、进污水管、酸碱加入管、混凝剂加入管、污水泵、第一连接管、第一排水管、溶气泵、进气嘴、第二排水管、第一助凝剂加入管、共聚反应器箱体、第二助凝剂加入管、搅拌机、搅拌杆、导流管、分离装置箱体、隔板、沉泥收集管、浮渣收集槽、净水收集管、第三连接管、净水收集箱和出水管;所述进污水管的一端位于所述污水池内,另一端与所述污水泵的进水口连接,所述酸碱加入管和混凝剂加入管均接入所述进污水管,所述第一连接管的一端与所述污水泵的出水口连接,另一端位于所述共聚反应器箱体内的下部,所述第一排水管的一端与所述污水泵的出水口连接,另一端与所述溶气泵的进水口连接,所述进气嘴与所述溶气泵的进气口连接,所述第二排水管的一端与所述溶气泵的出水口连接,另一端与所述第一连接管连接,所述第一助凝剂加入管接入所述第一连接管,所述第二助凝剂加入管接入所述共聚反应器箱体的中部,所述搅拌机的搅拌杆位于所述共聚反应器箱体内,所述隔板和沉泥收集管均设在所述分离装置箱体内,所述隔板为上下开口的倒锥状,所述沉泥收集管的上端开口与所述隔板的下端开口位置对应且留有间隙,所述导流管的一端与所述共聚反应器箱体的上端连接,另一端位于所述隔板的中心位置,所述分离装置箱体的上部设有浮渣收集槽,所述净水收集管的一端位于所述分离装置箱体内的下部,另一端通过所述第三连接管与所述净水收集箱连接,所述出水管与所述净水收集箱的底部连接。In order to solve the above technical problems, the utility model provides a coagulation air flotation copolymerization quick separation device, including a sewage tank, a sewage inlet pipe, an acid-base adding pipe, a coagulant adding pipe, a sewage pump, a first connecting pipe, a second One drain pipe, dissolved air pump, air inlet nozzle, second drain pipe, first coagulant aid adding pipe, copolymerization reactor box, second coagulant aid adding pipe, mixer, stirring rod, draft tube, separation device box Body, clapboard, sediment collection pipe, scum collection tank, clean water collection pipe, third connecting pipe, clean water collection box and outlet pipe; one end of the sewage inlet pipe is located in the sewage pool, and the other end is connected to the The water inlet of the sewage pump is connected, the acid-base adding pipe and the coagulant adding pipe are connected to the sewage inlet pipe, one end of the first connecting pipe is connected to the water outlet of the sewage pump, and the other end is located at In the lower part of the copolymerization reactor box, one end of the first drain pipe is connected to the water outlet of the sewage pump, and the other end is connected to the water inlet of the dissolved air pump, and the air inlet nozzle is connected to the water outlet of the dissolved air pump. One end of the second drain pipe is connected to the water outlet of the dissolved air pump, the other end is connected to the first connecting pipe, and the first coagulant adding pipe is connected to the first Connecting pipe, the second coagulation aid adding pipe is connected to the middle part of the copolymerization reactor box, the stirring rod of the mixer is located in the copolymerization reactor box, and the partition plate and the sediment collection pipe are all provided with In the separation device box, the partition is an inverted cone with upper and lower openings, and the upper opening of the sediment collection pipe corresponds to the lower opening of the partition with a gap left. One end is connected to the upper end of the copolymerization reactor box, the other end is located at the center of the partition, the upper part of the separation device box is provided with a scum collection tank, and one end of the clean water collection pipe is located at the The other end of the lower part of the separation device box is connected to the clean water collection box through the third connecting pipe, and the water outlet pipe is connected to the bottom of the clean water collection box.

优选的,所述进污水管、酸碱加入管和混凝剂加入管上均设有调节阀。Preferably, the sewage inlet pipe, the acid-base adding pipe and the coagulant adding pipe are all provided with regulating valves.

优选的,所述第一助凝剂加入管上设有一个调节阀,所述第二助凝剂加入管上设有两个调节阀。Preferably, one regulating valve is provided on the first coagulation aid adding pipe, and two regulating valves are arranged on the second coagulant aid feeding pipe.

优选的,所述第一连接管上依次设有调节阀、流量计、调节阀、取样水龙头和调节阀。Preferably, the first connecting pipe is sequentially provided with a regulating valve, a flow meter, a regulating valve, a sampling faucet and a regulating valve.

优选的,所述第一排水管连接有第二连接管,所述第二连接管上设有调节阀,所述第一排水管在与所述第二连接管连接处的两侧均设有调节阀,所述第一排水管上还设有压力表,所述第二排水管上依次设有调节阀、流量计、压力表、取样水龙头和调节阀,所述进气嘴上设有进气调节阀和空气流量计。Preferably, the first drain pipe is connected with a second connecting pipe, the second connecting pipe is provided with a regulating valve, and both sides of the first drain pipe are connected with the second connecting pipe. Regulating valve, the first drain pipe is also provided with a pressure gauge, the second drain pipe is provided with a regulating valve, a flow meter, a pressure gauge, a sampling faucet and a regulating valve in sequence, and the inlet nozzle is provided with an inlet Air regulating valve and air flow meter.

优选的,所述搅拌杆的下部设有第一搅拌叶片,所述搅拌杆的中部设有第二搅拌叶片。Preferably, the lower part of the stirring rod is provided with a first stirring blade, and the middle part of the stirring rod is provided with a second stirring blade.

优选的,所述浮渣收集槽的下部设有出浮渣管。Preferably, a scum outlet pipe is provided at the lower part of the scum collection tank.

优选的,所述分离装置箱体的下部设有排空管,所述排空管上设有调节阀。Preferably, an emptying pipe is provided at the lower part of the separation device box, and a regulating valve is provided on the emptying pipe.

优选的,所述净水收集管在所述分离装置箱体内的部分为穿孔管。Preferably, the part of the clean water collecting pipe inside the tank of the separation device is a perforated pipe.

优选的,所述净水收集箱内设有水位调整塞和湾流管,所述湾流管与所述第三连接管连接。Preferably, a water level adjustment plug and a gulf stream tube are provided in the clean water collection tank, and the gulf stream tube is connected to the third connecting pipe.

本实用新型的混凝气浮共聚快速分离装置能够有效处理经混凝沉淀池处理后的污水中残留的杂质,处理操作简单,处理成本低,可有效去除污水中的悬浮颗粒、乳化油、纤维、重金属等杂质,环保无污染,具有广阔的市场前景和应用价值。充分运用了混凝气浮共凝聚的基本原理,通过污水泵前加药混合和多项介质泵的溶气释气系统释放出密集的超微气泡,再加上助凝剂的加入生成絮体,带气絮体发生架桥、包卷、网捕作用,这三种结合方式形成的共聚复合体在上浮过程中,不但不会受到剪切力影响而使气泡脱落,浮渣十分稳定,并且含水率大大降低,而且由于形成的共聚复合体直径比传统的气浮大很多,与水的密度差也增大许多,根据斯托克斯定律,上浮速度与粒径的平方成正比,与颗粒与水的密度差成正比,所以,上浮速度比传统的气浮快,缩短反应分离时间,这样大大提高了气浮设备的分离效率与稳定性。助凝剂通过先后加到系统内,提高吸附架桥功能,使加入的助凝剂PAM水、气三者更迅速、均匀地有效混合,形成较大气泡与絮粒的共聚复合体,为共聚复合体的生成提供了有利的物化空间,提高上浮絮渣的稳定性与上浮能力。固液分离区上端隔板设置围成的倒锥形,倒锥形下端口与污泥收集管上端连接,混合液通过固液分离反应区内混凝气浮的作用,倒锥形隔板有效地使浮渣易于自动上浮分布到分离区液面上进入浮渣收集槽,而阻挡了将净化收集区的净水与浮渣混合,便于混合液的混合分离。出水通过调节水位调整塞控制分离装置箱体的排浮渣,实现浮渣在固液分离区内的浓缩脱水,能够进一步降低絮渣的含水率,简易方便。利用多项介质溶气泵将药、气-固-液三相在共聚反应区混凝共聚同步一体化,简化流程,并可产生稳定的气固液三相絮凝体,提高气浮效率、稳定气浮效果;采用左右混凝气浮共聚分离一体化方法与装置,占地面积小,可实现快速混凝共聚气浮,降低溶气能耗,提高气浮效率,简化气浮工艺流程。本实用新型的混凝气浮共聚快速分离装置可以用来处理生产生活过程中产生污水与废水中的胶体和悬浮物,完成固液分离。The coagulation air flotation copolymerization rapid separation device of the utility model can effectively treat the residual impurities in the sewage treated by the coagulation sedimentation tank, the treatment operation is simple, the treatment cost is low, and the suspended particles, emulsified oil and fibers in the sewage can be effectively removed , heavy metals and other impurities, environmental protection and pollution-free, has broad market prospects and application value. Make full use of the basic principle of coagulation, air flotation and co-coagulation, release dense ultra-micro bubbles through the pre-dosing and mixing of sewage pumps and the dissolved air release system of multiple media pumps, and add coagulation aids to form flocs , the bridging, enveloping, and netting effects of the air-bearing flocs occur. The copolymer complex formed by these three combinations will not only not be affected by the shear force and cause the air bubbles to fall off during the floating process, but the scum is very stable, and The water content is greatly reduced, and because the diameter of the formed copolymer complex is much larger than that of the traditional air flotation, the density difference with water is also much larger. According to Stokes' law, the floating speed is proportional to the square of the particle size, and is proportional to the particle size. It is directly proportional to the density difference of water, so the floating speed is faster than the traditional air flotation, shortening the reaction and separation time, which greatly improves the separation efficiency and stability of the air flotation equipment. The coagulant aid is added to the system successively to improve the adsorption and bridging function, so that the added coagulant aid PAM water and air can be mixed more quickly and evenly to form a copolymer complex of larger bubbles and flocs, which is called copolymerization. The formation of the complex provides a favorable physical and chemical space, and improves the stability and floating ability of the floating scum. The upper partition of the solid-liquid separation area is set to form an inverted cone, and the lower port of the inverted cone is connected to the upper end of the sludge collection pipe. The mixed liquid passes through the coagulation and air flotation in the solid-liquid separation reaction area, and the inverted cone partition is effective. The scum is easy to automatically float up and distribute to the liquid surface of the separation area and enter the scum collection tank, which prevents the mixing of the clean water in the purification collection area and the scum, and facilitates the mixing and separation of the mixed liquid. The outlet water controls the scum discharge of the separation device box by adjusting the water level adjustment plug to realize the concentration and dehydration of the scum in the solid-liquid separation area, which can further reduce the moisture content of the scum, which is simple and convenient. A number of medium-dissolved air pumps are used to synchronously integrate the drug, gas-solid-liquid three-phase coagulation and copolymerization in the copolymerization reaction zone, simplify the process, and produce stable gas-solid-liquid three-phase flocs, improve air flotation efficiency, stabilize gas Floatation effect: The left and right coagulation, air flotation, copolymerization and separation integration methods and devices are adopted, which occupy a small area and can realize rapid coagulation, copolymerization and air flotation, reduce the energy consumption of dissolved air, improve the efficiency of air flotation, and simplify the air flotation process. The coagulation air flotation copolymerization rapid separation device of the utility model can be used to treat colloids and suspended matter in sewage and waste water produced in the production and living process, and complete solid-liquid separation.

附图说明Description of drawings

图1为本实用新型实施例的混凝气浮共聚快速分离装置的结构示意图。Fig. 1 is a schematic structural view of a coagulation air flotation copolymerization quick separation device according to an embodiment of the present invention.

图中,1:污水池;2:进污水管;3:调节阀;4:酸碱加入管;5:混凝剂加入管;6:污水泵;7:调节阀;8:污水流量计;9:调节阀;10:取样水龙头;11:第一连接管;12:调节阀;13:调节阀;14:第二连接管;15:调节阀;16:真空表;17:空气流量计;18:进气调节阀;19:进气嘴;20:溶气泵;21:调节阀;22:溶气水流量计;23:压力表;24:取样水龙头;25:调节阀;26:第一助凝剂加入管;27:调节阀;28:第二助凝剂加入管;29:调节阀;30:搅拌机;31:搅拌杆;32:第二搅拌叶片;33:第一搅拌叶片;34:导流管;35:隔板;36:沉泥收集管;37:浮渣收集槽;38:净水收集管;39:第三连接管;40:水位调整塞;41:弯流管;42:出水管;43:分离装置箱体;44:共聚反应器箱体;45:出浮渣管;46:排空管;101:共聚反应区;102:固液分离区;103:净水收集区;104:水位调整区。In the figure, 1: sewage pool; 2: sewage inlet pipe; 3: regulating valve; 4: acid-base adding pipe; 5: coagulant adding pipe; 6: sewage pump; 7: regulating valve; 8: sewage flowmeter; 9: regulating valve; 10: sampling faucet; 11: first connecting pipe; 12: regulating valve; 13: regulating valve; 14: second connecting pipe; 15: regulating valve; 16: vacuum gauge; 17: air flow meter; 18: Air intake regulating valve; 19: Air intake nozzle; 20: Dissolved air pump; 21: Regulating valve; 22: Dissolved air water flow meter; 23: Pressure gauge; 24: Sampling faucet; 25: Regulating valve; 26: First Coagulant aid adding pipe; 27: regulating valve; 28: second coagulant aid adding pipe; 29: regulating valve; 30: mixer; 31: stirring rod; 32: second stirring blade; 33: first stirring blade; 34 : diversion pipe; 35: clapboard; 36: sediment collection pipe; 37: scum collection tank; 38: clean water collection pipe; 39: third connecting pipe; 40: water level adjustment plug; 41: elbow pipe; 42: water outlet pipe; 43: separation device box; 44: copolymerization reactor box; 45: scum outlet pipe; 46: emptying pipe; 101: copolymerization reaction area; 102: solid-liquid separation area; 103: water purification collection area; 104: water level adjustment area.

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,但不能用来限制本实用新型的范围。The implementation of the present utility model will be further described in detail below in conjunction with the accompanying drawings and examples. The following examples are used to illustrate the utility model, but cannot be used to limit the scope of the utility model.

在本实用新型的描述中,需要说明的是,术语“中心”、“纵向”、“横向”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制。此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present utility model, it should be noted that the terms "center", "longitudinal", "transverse", "upper", "lower", "front", "rear", "left", "right", The orientations or positional relationships indicated by "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. are based on the orientation or positional relationships shown in the drawings, and are only for the convenience of describing the present invention. Novel and simplified descriptions do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be construed as limiting the utility model. In addition, the terms "first" and "second" are used for descriptive purposes only, and should not be understood as indicating or implying relative importance.

在本实用新型的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本实用新型中的具体含义。此外,在本实用新型的描述中,除非另有说明,“多个”的含义是两个或两个以上。In the description of the present utility model, it should be noted that, unless otherwise clearly stipulated and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a flexible connection. Detachable connection, or integral connection; it can be mechanical connection or electrical connection; it can be direct connection or indirect connection through an intermediary, and it can be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present utility model in specific situations. In addition, in the description of the present utility model, unless otherwise specified, "plurality" means two or more.

如图1所示,本实施例的混凝气浮共聚快速分离装置包括:污水池1、进污水管2、酸碱加入管4、混凝剂加入管5、污水泵6、第一连接管11、第一排水管、溶气泵20、进气嘴19、第二排水管、第一助凝剂加入管26、共聚反应器箱体44、第二助凝剂加入管28、搅拌机30、搅拌杆31、导流管34、分离装置箱体43、隔板35、沉泥收集管36、浮渣收集槽37、净水收集管38、第三连接管39、净水收集箱和出水管42。As shown in Figure 1, the coagulation air flotation copolymerization rapid separation device of this embodiment includes: a sewage tank 1, a sewage inlet pipe 2, an acid-base adding pipe 4, a coagulant adding pipe 5, a sewage pump 6, a first connecting pipe 11. The first drainage pipe, the dissolved air pump 20, the air inlet nozzle 19, the second drainage pipe, the first coagulant aid adding pipe 26, the copolymerization reactor box 44, the second coagulant aid adding pipe 28, the mixer 30, the stirring Rod 31, diversion pipe 34, separation device box 43, partition 35, sediment collection pipe 36, scum collection tank 37, clean water collection pipe 38, third connecting pipe 39, clean water collection box and outlet pipe 42 .

进污水管2的一端位于污水池1内,另一端与污水泵6的进水口连接,酸碱加入管4和混凝剂加入管5均接入进污水管2,第一连接管11的一端与污水泵6的出水口连接,另一端位于共聚反应器箱体44内的下部,第一排水管的一端与污水泵6的出水口连接,另一端与溶气泵20的进水口连接,进气嘴19与溶气泵20的进气口连接,第二排水管的一端与溶气泵20的出水口连接,另一端与第一连接管11连接,第一助凝剂加入管26接入第一连接管11,第二助凝剂加入管28接入共聚反应器箱体44的中部,搅拌机30的搅拌杆31位于共聚反应器箱体44内,隔板35和沉泥收集管36均设在分离装置箱体43内,隔板为上下开口的倒锥状,沉泥收集管36的上端开口与隔板35的下端开口位置对应且留有间隙,导流管34的一端与共聚反应器箱体44的上端连接,另一端位于隔板35的中心位置,分离装置箱体43的上部设有浮渣收集槽37,净水收集管38的一端位于分离装置箱体43内的下部,另一端通过第三连接管39与净水收集箱连接,出水管42与净水收集箱的底部连接。One end of the sewage inlet pipe 2 is located in the sewage pool 1, the other end is connected to the water inlet of the sewage pump 6, the acid-base adding pipe 4 and the coagulant adding pipe 5 are connected to the sewage pipe 2, and one end of the first connecting pipe 11 It is connected with the water outlet of the sewage pump 6, and the other end is located at the bottom of the copolymerization reactor box 44. One end of the first drain pipe is connected with the water outlet of the sewage pump 6, and the other end is connected with the water inlet of the dissolved air pump 20, and the air intake The nozzle 19 is connected to the air inlet of the dissolved air pump 20, one end of the second drain pipe is connected to the water outlet of the dissolved air pump 20, the other end is connected to the first connecting pipe 11, and the first coagulant adding pipe 26 is connected to the first connecting pipe. Pipe 11, the second coagulation aid adding pipe 28 are connected to the middle part of the copolymerization reactor box 44, the stirring rod 31 of the mixer 30 is located in the copolymerization reactor box 44, and the dividing plate 35 and the sludge collection pipe 36 are all arranged at the separation In the device box 43, the partition is an inverted conical shape with upper and lower openings, the upper opening of the sediment collection pipe 36 corresponds to the lower opening of the partition 35 and there is a gap, and one end of the draft pipe 34 is connected to the copolymerization reactor box. The upper end of 44 is connected, and the other end is positioned at the central position of dividing plate 35, and the top of separator casing 43 is provided with scum collecting tank 37, and one end of clean water collecting pipe 38 is positioned at the bottom in separator casing 43, and the other end passes through The third connecting pipe 39 is connected with the clean water collection box, and the water outlet pipe 42 is connected with the bottom of the clean water collection box.

进污水管2上设有调节阀3,酸碱加入管4和混凝剂加入管5上均设有调节阀。第一助凝剂加入管26上设有一个调节阀,第二助凝剂加入管28上设有两个调节阀。第一连接管11上依次设有调节阀7、流量计8、调节阀9、取样水龙头10和调节阀27。第一排水管连接有第二连接管14,第二连接管14上设有调节阀13,第一排水管在与第二连接管14连接处的两侧分别设有调节阀12和调节阀15,第一排水管上还设有压力表16,第二排水管上依次设有调节阀21、流量计22、压力表23、取样水龙头24和调节阀25,进气嘴19上设有进气调节阀18和空气流量计17。搅拌杆31的下部设有第一搅拌叶片33,搅拌杆31的中部设有第二搅拌叶片32。浮渣收集槽37的下部设有出浮渣管45。分离装置箱体43的下部设有排空管46,排空管46上设有调节阀。净水收集管38在分离装置箱体43内的部分为穿孔管。净水收集箱内设有水位调整塞40和湾流管41,湾流管41与第三连接管39连接。The sewage inlet pipe 2 is provided with a regulating valve 3, and the acid-base adding pipe 4 and the coagulant adding pipe 5 are all provided with regulating valves. The first coagulant aid adding pipe 26 is provided with a regulating valve, and the second coagulant aid feeding pipe 28 is provided with two regulating valves. A regulating valve 7 , a flow meter 8 , a regulating valve 9 , a sampling faucet 10 and a regulating valve 27 are sequentially provided on the first connecting pipe 11 . The first drain pipe is connected with a second connecting pipe 14, the second connecting pipe 14 is provided with a regulating valve 13, and the first drain pipe is respectively provided with a regulating valve 12 and a regulating valve 15 on both sides of the joint with the second connecting pipe 14 , the first drain pipe is also provided with a pressure gauge 16, the second drain pipe is provided with a regulating valve 21, a flow meter 22, a pressure gauge 23, a sampling faucet 24 and a regulating valve 25 in sequence, and the air inlet nozzle 19 is provided with an air inlet Regulating valve 18 and air flow meter 17. The lower part of the stirring rod 31 is provided with a first stirring blade 33 , and the middle part of the stirring rod 31 is provided with a second stirring blade 32 . The bottom of the scum collection tank 37 is provided with a scum outlet pipe 45 . The bottom of the separation device box 43 is provided with an emptying pipe 46 , and a regulating valve is arranged on the emptying pipe 46 . The part of the clean water collecting pipe 38 in the separating device casing 43 is a perforated pipe. A water level adjustment plug 40 and a gulf stream pipe 41 are arranged in the clean water collecting tank, and the gulf stream pipe 41 is connected with the third connecting pipe 39 .

本实施例的混凝气浮共聚快速分离装置,可以划分为:共聚反应区101、固液分离区102、净水收集区103、水位调整区104,通过设置独立的共聚反应系统、独立的固液分离系统来实现混凝气浮共聚气浮分离过程的优化,同时在排浮渣方式上采用变水位排渣方式,简易便捷,整套设备占地小、投资少、效率高。The coagulation air flotation copolymerization rapid separation device of this embodiment can be divided into: copolymerization reaction zone 101, solid-liquid separation zone 102, clean water collection zone 103, water level adjustment zone 104, by setting independent copolymerization reaction system, independent solid The liquid separation system is used to realize the optimization of the coagulation air flotation copolymerization air flotation separation process. At the same time, the variable water level slag discharge method is adopted in the scum discharge method, which is simple and convenient. The whole set of equipment occupies a small area, requires less investment and has high efficiency.

污水加药混合系统由污水泵6、混凝剂加入管5、酸或碱加入管4、助凝剂PAM加入管26和28、助凝剂PAM加入管28、流量计8、调节阀3/7/9、取样水龙头10组成;混凝剂、pH调节剂通过污水泵6的自吸作用吸入,加药量由阀4和阀5控制,经过水泵的叶轮的高速旋转切割,使药液与污水混合,污水泵的出水管连管道11依次接调节阀7、流量计8、调节阀9、取样水龙头10和溶气泵出水管,助凝剂加入管26通过调节阀控制加入到污水与溶气水混合后的加药点;助凝剂PAM加入管28通过调节阀29控制加入共聚反应区。The sewage dosing and mixing system consists of sewage pump 6, coagulant adding pipe 5, acid or alkali adding pipe 4, coagulant PAM adding pipe 26 and 28, coagulant aid PAM adding pipe 28, flow meter 8, regulating valve 3/ 7/9, composed of sampling tap 10; coagulant and pH regulator are sucked in by the self-priming action of sewage pump 6, and the dosing amount is controlled by valve 4 and valve 5, and the high-speed rotating cutting of the impeller of the water pump makes the liquid medicine and Sewage is mixed, the outlet pipe of the sewage pump is connected with the pipeline 11 in turn to the regulating valve 7, the flow meter 8, the regulating valve 9, the sampling faucet 10 and the outlet pipe of the dissolved air pump, and the coagulant adding pipe 26 is controlled to add sewage and dissolved air through the regulating valve The dosing point after the water is mixed; the coagulant aid PAM adding pipe 28 is controlled to be added to the copolymerization reaction zone through the regulating valve 29 .

多项介质泵溶气系统由溶气泵20、流量计22、压力表23、取样水龙头24、阀等组成;溶气泵把污水泵6输出后的污水管中的污水吸入泵体,通过调节阀12/13/14/15控制流量,并在溶气泵进气嘴19处通过泵前的空气流量计17和进气调节阀18吸入空气,空气经溶气泵被反复切割后,压力维持在0.3-0.5Mpa范围内,根据共聚的特性以及微气泡释放过程特征,通过调节阀使分散溶入水中的空气快速放出,保证释放出的微小气泡直径在1-10微米,压力由压力表30显示,通过溶气水流量计22控制加入量,与加药混合后的污水相汇,汇合后再与助凝剂加药管26加入的助凝剂PAM汇合,汇合后通过管道进入到共聚反应区a底部。Multi-media pump dissolved air system is composed of dissolved air pump 20, flow meter 22, pressure gauge 23, sampling faucet 24, valves, etc.; /13/14/15 Control the flow, and inhale air through the air flow meter 17 and the air intake regulating valve 18 in front of the pump at the inlet nozzle 19 of the dissolved air pump. After the air is repeatedly cut by the dissolved air pump, the pressure is maintained at 0.3-0.5 Within the range of Mpa, according to the characteristics of the copolymerization and the characteristics of the microbubble release process, the air dispersed and dissolved in the water can be released quickly through the regulating valve to ensure that the diameter of the microbubbles released is 1-10 microns, and the pressure is displayed by the pressure gauge 30. The air-water flowmeter 22 controls the addition amount, and merges with the mixed sewage after the dosing, and then merges with the coagulant PAM added by the coagulant dosing pipe 26, and enters the bottom of the copolymerization reaction zone a through the pipeline after confluence.

共聚反应系统由共聚反应箱体44、混合液进水管与阀27、助凝剂加入管与阀28/29、搅拌机30、搅拌杆31、搅拌叶片32/33、出水导流管34组成;溶汽水加药混合液从箱体底部进入,遇搅拌叶片33开始旋流混合,到箱体中间部位时与助凝剂PAM相遇,再通过搅拌叶片32搅拌充分混合,箱体上部已混合均匀的水通过出水导流管32与共聚反应区液面位置相连,整体与箱体成60度倾斜伸向固液分离区沉淀收集管的上端。The copolymerization reaction system is composed of a copolymerization reaction box 44, a mixed liquid inlet pipe and a valve 27, a coagulation aid adding pipe and a valve 28/29, a mixer 30, a stirring rod 31, a stirring blade 32/33, and a water outlet guide pipe 34; The soda water dosing mixture enters from the bottom of the box, and starts to swirl and mix when it meets the stirring blade 33. When it reaches the middle of the box, it meets the coagulant PAM, and then is fully mixed by the stirring blade 32. The water that has been evenly mixed in the upper part of the box The water outlet guide pipe 32 is connected to the liquid level in the copolymerization reaction zone, and the whole body is inclined at 60 degrees to the upper end of the precipitation collection pipe in the solid-liquid separation zone.

固液分离系统包含固液分离区b、净水收集区c、水位调整区d;固液分离区b由上端隔板35和下端污泥收集管36组成,隔板与污泥收集管连接位置设有溢流口,净水区c由上端浮渣收集槽37和底部净水收集管38组成;来水通过导流管34在固液分离区b的上端隔板围成的倒锥形的中心位置进水,混合液进入污泥收集管36后通过气浮使混凝后的絮粒上浮到浮渣收集槽37,以此实现快速的固液分离,而较重的絮体悬浮物在污泥收集槽36中沉淀,通过底部排空管与阀46去除,净水从污泥收集管36上端溢流口溢出到净水收集区c,净水收集区下部的净水收集管38与出水管39的下端相连,净水由此进入分离装置箱体43外侧的水位调整区内d,其内设有水位调整塞40、弯流管41和出水管42,当分离装置箱体43内水位升高或降低时,可调节水位调整塞40调整到适当水位,此时关闭水位调整塞,水从弯流管41流出,通过出水管42排出。装置底部外侧安装有支腿。The solid-liquid separation system includes a solid-liquid separation area b, a clean water collection area c, and a water level adjustment area d; the solid-liquid separation area b is composed of an upper partition 35 and a lower sludge collection pipe 36, and the connection position between the partition and the sludge collection pipe is An overflow port is provided, and the clean water area c is composed of the upper end scum collection tank 37 and the bottom clean water collection pipe 38; the incoming water passes through the diversion pipe 34 and is surrounded by the upper end partition of the solid-liquid separation area b. Water enters the central position, and the mixed liquid enters the sludge collection pipe 36, and then the coagulated flocs float to the scum collection tank 37 through air flotation, so as to realize rapid solid-liquid separation, while the heavier floc suspended matter is The sediment in the sludge collection tank 36 is removed through the bottom emptying pipe and valve 46, and the clean water overflows from the overflow port at the upper end of the sludge collection pipe 36 to the clean water collection area c, and the clean water collection pipe 38 at the bottom of the clean water collection area is connected to the The lower ends of the water outlet pipe 39 are connected, and the clean water enters the water level adjustment area d on the outside of the separation device casing 43. A water level adjustment plug 40, an elbow pipe 41 and a water outlet pipe 42 are arranged in it. When the water level rises or falls, the adjustable water level adjustment plug 40 is adjusted to an appropriate water level. At this time, the water level adjustment plug is closed, and the water flows out from the elbow 41 and is discharged through the outlet pipe 42. Outriggers are installed on the outside of the bottom of the device.

本实施例的混凝气浮共聚快速分离装置的工作原理包括:The working principle of the coagulation air flotation copolymerization quick separation device of the present embodiment includes:

A、加药混合系统:混凝剂、pH调节剂通过污水泵自吸作用吸入,加药量由流量计控制,经过水泵的叶轮的高速旋转切割,使药液与污水混合,出水管连接流量计、调节阀、压力表、取样水龙头,助凝剂通过调节阀控制加入到混合反应系统内的加药点;A. Dosing and mixing system: the coagulant and pH regulator are sucked in through the self-priming action of the sewage pump, the dosing amount is controlled by the flow meter, and the high-speed rotating cutting of the impeller of the water pump makes the medicine liquid mix with the sewage, and the outlet pipe connects the flow rate Gauge, regulating valve, pressure gauge, sampling faucet, coagulant aid is controlled by the regulating valve to the dosing point added to the mixed reaction system;

B、多项介质泵溶气系统:溶气泵入水管与污水泵出水管的连接点连接,通过阀控制流量,溶气泵吸入管路上与其平行位置上空气进气嘴,通过近期流量计和调节阀定量空气,空气被污水泵反复切割后,使气体分散溶入污水中,压力维持在0.2-0.3Mpa范围内,溶汽水出水管连接流量计、调节阀、压力表、取样水龙头,与污水泵出水管加药点前端汇合,加药污水和溶气水在一起通过连接的助凝剂加药点加入的助凝剂混合反应形成较大粒径的气泡与絮粒的共聚复合体,进入共聚反应内进行混凝共聚。B. Multi-media pump dissolved air system: the connection point between the water inlet pipe of the dissolved air pump and the outlet pipe of the sewage pump is connected, and the flow is controlled by a valve. Quantitative air, the air is repeatedly cut by the sewage pump, so that the gas is dispersed and dissolved in the sewage, and the pressure is maintained within the range of 0.2-0.3Mpa. The dissolved steam water outlet pipe is connected with a flow meter, a regulating valve, a pressure gauge, and a sampling faucet, and is pumped out with the sewage The front end of the water pipe dosing point converges, and the dosing sewage and dissolved air water are mixed and reacted together through the coagulant aid added at the connected coagulant dosing point to form a copolymerization complex of larger particle size air bubbles and flocs, which enters the copolymerization reaction Internal coagulation and copolymerization.

C、共聚反应系统:加药混合后的溶汽水进入共聚反应区的共聚反应器箱体底部自下而上流入,同时在共聚反应器箱体中部再由助凝剂加入管控制加入PAM,在搅拌机带动下通过搅拌杆和搅拌叶片的作用,使加入的助凝剂PAM水、气三者更迅速、均匀地有效混合,形成较大气泡与絮粒的共聚复合体,通过导流管溢流进入固液分离内进行分离。C. Copolymerization reaction system: The dissolved gas water after dosing and mixing enters the bottom of the copolymerization reactor box in the copolymerization reaction zone and flows from bottom to top, and at the same time, in the middle of the copolymerization reactor box, PAM is controlled by the coagulant adding pipe, and then Driven by the mixer, through the action of the stirring rod and the stirring blade, the added coagulant PAM water and air are mixed more quickly and evenly, forming a copolymer complex of larger air bubbles and flocs, which overflows through the diversion tube Enter the solid-liquid separation for separation.

D、固液分离系统:完成药水混合絮凝后并形成较大粒径的气泡与絮粒的共聚复合体的混合体通过导流管溢流进入固液分离区内,导流管在固液分离区上端隔板围成的倒锥形的中心位置进水,倒锥形下端口与污泥收集管上端连接,混合液进入污泥收集管后,形成较大气泡与絮粒的共聚复合体的密度与水的密度差较大,粒径比原污水中的颗粒大许多,会自动上升到分离区顶部,形成浮渣层实现快速的固液分离,浮渣通过收集槽和排泥管排出;而底泥通过底部排空管与阀去除;分离的净水从收集管上端溢流口溢出到净水收集区,净水收集区下部安装有穿孔集水管,穿孔集水管与出水管的下端相连,出水通过出水管进入分离装置箱体外侧的水位调整区,调整适当水位后,关闭水位调整塞,水从弯流管流出,净水通过排水出水管排出。D. Solid-liquid separation system: After the mixing and flocculation of the liquid medicine is completed, the mixture of large-sized air bubbles and flocculent copolymer complexes will overflow into the solid-liquid separation area through the diversion tube, and the diversion tube will be in the solid-liquid separation Water enters the center of the inverted cone surrounded by the partition at the upper end of the area, and the lower port of the inverted cone is connected to the upper end of the sludge collection pipe. After the mixed solution enters the sludge collection pipe, it forms a copolymer complex of larger air bubbles and flocs. The difference between the density and the density of water is large, and the particle size is much larger than the particles in the raw sewage, which will automatically rise to the top of the separation zone, forming a scum layer to achieve rapid solid-liquid separation, and the scum is discharged through the collection tank and the sludge discharge pipe; The bottom mud is removed through the bottom emptying pipe and valve; the separated clean water overflows from the overflow at the upper end of the collecting pipe to the clean water collection area, and the lower part of the clean water collection area is equipped with a perforated water collection pipe, which is connected to the lower end of the outlet pipe , the outlet water enters the water level adjustment area outside the separation device box through the outlet pipe, after adjusting the appropriate water level, close the water level adjustment plug, the water flows out from the curved flow pipe, and the clean water is discharged through the drain outlet pipe.

本实用新型的混凝气浮共聚快速分离装置能够有效处理经混凝沉淀池处理后的污水中残留的杂质,处理操作简单,处理成本低,可有效去除污水中的悬浮颗粒、乳化油、纤维、重金属等杂质,环保无污染,具有广阔的市场前景和应用价值。充分运用了混凝气浮共凝聚的基本原理,通过污水泵前加药混合和多项介质泵的溶气释气系统释放出密集的超微气泡,再加上助凝剂的加入生成絮体,带气絮体发生架桥、包卷、网捕作用,这三种结合方式形成的共聚复合体在上浮过程中,不但不会受到剪切力影响而使气泡脱落,浮渣十分稳定,并且含水率大大降低,而且由于形成的共聚复合体直径比传统的气浮大很多,与水的密度差也增大许多,根据斯托克斯定律,上浮速度与粒径的平方成正比,与颗粒与水的密度差成正比,所以,上浮速度比传统的气浮快,缩短反应分离时间,这样大大提高了气浮设备的分离效率与稳定性。助凝剂通过先后加到系统内,提高吸附架桥功能,使加入的助凝剂PAM水、气三者更迅速、均匀地有效混合,形成较大气泡与絮粒的共聚复合体,为共聚复合体的生成提供了有利的物化空间,提高上浮絮渣的稳定性与上浮能力。固液分离区上端隔板设置围成的倒锥形,倒锥形下端口与污泥收集管上端连接,混合液通过固液分离反应区内混凝气浮的作用,倒锥形隔板有效地使浮渣易于自动上浮分布到分离区液面上进入浮渣收集槽,而阻挡了将净化收集区的净水与浮渣混合,便于混合液的混合分离。出水通过调节水位调整塞控制分离装置箱体的排浮渣,实现浮渣在固液分离区内的浓缩脱水,能够进一步降低絮渣的含水率,简易方便。利用多项介质溶气泵将药、气-固-液三相在共聚反应区混凝共聚同步一体化,简化流程,并可产生稳定的气固液三相絮凝体,提高气浮效率、稳定气浮效果;采用左右混凝气浮共聚分离一体化方法与装置,占地面积小,可实现快速混凝共聚气浮,降低溶气能耗,提高气浮效率,简化气浮工艺流程。本实用新型的混凝气浮共聚快速分离装置可以用来处理生产生活过程中产生污水与废水中的胶体和悬浮物,完成固液分离。The coagulation air flotation copolymerization rapid separation device of the utility model can effectively treat the residual impurities in the sewage treated by the coagulation sedimentation tank, the treatment operation is simple, the treatment cost is low, and the suspended particles, emulsified oil and fibers in the sewage can be effectively removed , heavy metals and other impurities, environmental protection and pollution-free, has broad market prospects and application value. Make full use of the basic principle of coagulation, air flotation and co-coagulation, release dense ultra-micro bubbles through the pre-dosing and mixing of sewage pumps and the dissolved air release system of multiple media pumps, and add coagulation aids to form flocs , the bridging, enveloping, and netting effects of the air-bearing flocs occur. The copolymer complex formed by these three combinations will not only not be affected by the shear force and cause the air bubbles to fall off during the floating process, but the scum is very stable, and The water content is greatly reduced, and because the diameter of the formed copolymer complex is much larger than that of the traditional air flotation, the density difference with water is also much larger. According to Stokes' law, the floating speed is proportional to the square of the particle size, and is proportional to the particle size. It is directly proportional to the density difference of water, so the floating speed is faster than the traditional air flotation, shortening the reaction and separation time, which greatly improves the separation efficiency and stability of the air flotation equipment. The coagulant aid is added to the system successively to improve the adsorption and bridging function, so that the added coagulant aid PAM water and air can be mixed more quickly and evenly to form a copolymer complex of larger bubbles and flocs, which is called copolymerization. The formation of the complex provides a favorable physical and chemical space, and improves the stability and floating ability of the floating scum. The upper partition of the solid-liquid separation area is set to form an inverted cone, and the lower port of the inverted cone is connected to the upper end of the sludge collection pipe. The mixed liquid passes through the coagulation and air flotation in the solid-liquid separation reaction area, and the inverted cone partition is effective. The scum is easy to automatically float up and distribute to the liquid surface of the separation area and enter the scum collection tank, which prevents the mixing of the clean water in the purification collection area and the scum, and facilitates the mixing and separation of the mixed liquid. The outlet water controls the scum discharge of the separation device box by adjusting the water level adjustment plug to realize the concentration and dehydration of the scum in the solid-liquid separation area, which can further reduce the moisture content of the scum, which is simple and convenient. A number of medium-dissolved air pumps are used to synchronously integrate the drug, gas-solid-liquid three-phase coagulation and copolymerization in the copolymerization reaction zone, simplify the process, and produce stable gas-solid-liquid three-phase flocs, improve air flotation efficiency, stabilize gas Floatation effect: The left and right coagulation, air flotation, copolymerization and separation integration methods and devices are adopted, which occupy a small area and can realize rapid coagulation, copolymerization and air flotation, reduce the energy consumption of dissolved air, improve the efficiency of air flotation, and simplify the air flotation process. The coagulation air flotation copolymerization rapid separation device of the utility model can be used to treat colloids and suspended matter in sewage and waste water produced in the production and living process, and complete solid-liquid separation.

本实用新型的实施例是为了示例和描述起见而给出的,而并不是无遗漏的或者将本实用新型限于所公开的形式。很多修改和变化对于本领域的普通技术人员而言是显而易见的。选择和描述实施例是为了更好说明本实用新型的原理和实际应用,并且使本领域的普通技术人员能够理解本实用新型从而设计适于特定用途的带有各种修改的各种实施例。The embodiments of the invention have been presented for purposes of illustration and description, but are not intended to be exhaustive or to limit the invention to the forms disclosed. Many modifications and changes will be apparent to those of ordinary skill in the art. The embodiment was chosen and described in order to better explain the principle and practical application of the invention, and to enable those of ordinary skill in the art to understand the invention and design various embodiments with various modifications suitable for particular purposes.

Claims (10)

1. A coagulation air-flotation copolymerization quick separation device is characterized by comprising a sewage pool (1), a sewage inlet pipe (2), an acid-base adding pipe (4), a coagulant adding pipe (5), a sewage pump (6), a first connecting pipe (11), a first water discharge pipe, a dissolved air pump (20), an air inlet nozzle (19), a second water discharge pipe, a first coagulant aid adding pipe (26), a copolymerization reactor box body (44), a second coagulant aid adding pipe (28), a stirrer (30), a stirring rod (31), a guide pipe (34), a separation device box body (43), a partition plate (35), a settled sludge collecting pipe (36), a scum collecting tank (37), a purified water collecting pipe (38), a third connecting pipe (39), a purified water collecting box and a water outlet pipe (42); one end of the sewage inlet pipe (2) is positioned in the sewage pool (1), the other end of the sewage inlet pipe is connected with a water inlet of the sewage pump (6), the acid-base adding pipe (4) and the coagulant adding pipe (5) are connected into the sewage inlet pipe (2), one end of the first connecting pipe (11) is connected with a water outlet of the sewage pump (6), the other end of the first connecting pipe is positioned at the lower part of the copolymerization reactor box body (44), one end of the first water discharge pipe is connected with a water outlet of the sewage pump (6), the other end of the first water discharge pipe is connected with a water inlet of the dissolved air pump (20), the air inlet nozzle (19) is connected with an air inlet of the dissolved air pump (20), one end of the second water discharge pipe is connected with a water outlet of the dissolved air pump (20), the other end of the second water discharge pipe is connected with the first connecting pipe (11), the first coagulant adding pipe (26) is connected into the first, the second coagulant aid adding pipe (28) is connected to the middle part of the copolymerization reactor box body (44), a stirring rod (31) of the stirrer (30) is positioned in the copolymerization reactor box body (44), the partition plate (35) and the sludge settling collecting pipe (36) are arranged in the separation device box body (43), the partition plate is in an inverted cone shape with an upper opening and a lower opening, an upper opening of the sludge settling collecting pipe (36) corresponds to a lower opening of the partition plate (35) and is provided with a gap, one end of the flow guide pipe (34) is connected with the upper end of the copolymerization reactor box body (44), the other end of the flow guide pipe is positioned at the central position of the partition plate (35), a scum collecting tank (37) is arranged at the upper part of the separation device box body (43), one end of the water purifying collecting pipe (38) is positioned at the lower part of the separation device box body (43), and the other end of the water purifying collecting pipe is connected with the water purifying collecting, the water outlet pipe (42) is connected with the bottom of the purified water collecting box.
2. The coagulation air-flotation copolymerization rapid separation device according to claim 1, wherein the sewage inlet pipe (2), the acid-base adding pipe (4) and the coagulant adding pipe (5) are respectively provided with an adjusting valve.
3. The coagulation air-flotation copolymerization rapid separation device as claimed in claim 1, wherein the first coagulant aid addition pipe (26) is provided with one regulating valve, and the second coagulant aid addition pipe (28) is provided with two regulating valves.
4. The coagulation air-flotation copolymerization rapid separation device as claimed in claim 1, wherein the first connecting pipe (11) is provided with a regulating valve, a flow meter, a regulating valve, a sampling faucet and a regulating valve in sequence.
5. The coagulation air-flotation copolymerization rapid separation device according to claim 1, wherein the first drain pipe is connected with a second connecting pipe (14), the second connecting pipe (14) is provided with a regulating valve, the first drain pipe is provided with regulating valves on both sides of the joint with the second connecting pipe (14), the first drain pipe is further provided with a pressure gauge, the second drain pipe is provided with a regulating valve, a flow meter, a pressure gauge, a sampling faucet and a regulating valve in sequence, and the air inlet nozzle (19) is provided with an air inlet regulating valve (18) and an air flow meter (17).
6. The coagulation air-flotation copolymerization rapid separation device according to claim 1, wherein a first stirring blade (33) is provided at the lower part of the stirring rod (31), and a second stirring blade (32) is provided at the middle part of the stirring rod (31).
7. The coagulation air-flotation copolymerization rapid separation device according to claim 1, wherein the lower part of the scum collection tank (37) is provided with a scum outlet pipe (45).
8. The coagulation air-flotation copolymerization rapid separation device as claimed in claim 1, wherein an evacuation pipe (46) is provided at the lower part of the separation device box (43), and the evacuation pipe (46) is provided with a regulating valve.
9. The coagulation air-flotation copolymerization rapid separation device according to claim 1, wherein the part of the purified water collection pipe (38) in the separation device box body (43) is a perforated pipe.
10. The coagulation air-flotation copolymerization rapid separation device according to claim 1, wherein a water level adjusting plug (40) and a gulf stream pipe (41) are arranged in the water purification collection tank, and the gulf stream pipe (41) is connected with the third connecting pipe (39).
CN201920616766.0U 2019-04-30 2019-04-30 Coagulation air flotation copolymerization quick separation device Active CN209835843U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109956587A (en) * 2019-04-30 2019-07-02 大连交通大学 Coagulation and flotation copolymerization rapid separation system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109956587A (en) * 2019-04-30 2019-07-02 大连交通大学 Coagulation and flotation copolymerization rapid separation system
CN109956587B (en) * 2019-04-30 2023-09-22 大连交通大学 Quick separation system for coagulation air-floatation copolymerization

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