CN211620175U - Coagulation air flotation experiment system - Google Patents

Coagulation air flotation experiment system Download PDF

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CN211620175U
CN211620175U CN201922371267.2U CN201922371267U CN211620175U CN 211620175 U CN211620175 U CN 211620175U CN 201922371267 U CN201922371267 U CN 201922371267U CN 211620175 U CN211620175 U CN 211620175U
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pipe
coagulation
water
sewage
air flotation
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许芝
魏满奇
姜慧
费洪剑
邹之本
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Dalian Jiaotong University
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Abstract

本实用新型涉及环境工程水处理技术领域,具体公开了一种混凝气浮实验系统,包括加药混合系统、溶气气浮系统、混凝气浮反应系统和固液分离系统,加药混合系统包括PAM药箱、PAM计量泵、PAM加药管、PAC药箱、PAC计量泵、PAC加药管、酸碱药箱、酸碱计量泵、酸碱加药管、污水箱、污水进入管、污水泵和污水管,溶气气浮系统包括清水箱、进水管、溶气泵、出溶气水管、气体流量计和气体控制阀,混凝气浮反应系统包括混凝反应柱、可调节搅拌器和连接管,固液分离系统包括固液分离柱、水位调节阀、清水收集箱、清水收集管、浮渣排出管和清水排出管。本实用新型克服了占地面积大、能耗高、管理复杂、填料堵塞和损失水量大等问题。

Figure 201922371267

The utility model relates to the technical field of environmental engineering water treatment, and specifically discloses a coagulation and air flotation experiment system, which comprises a drug dosing and mixing system, a dissolved air flotation system, a coagulation air flotation reaction system and a solid-liquid separation system. The system includes PAM medicine box, PAM metering pump, PAM dosing pipe, PAC medicine box, PAC metering pump, PAC dosing pipe, acid-base medicine box, acid-base metering pump, acid-base dosing pipe, sewage tank, sewage inlet pipe , sewage pump and sewage pipe, dissolved air flotation system includes clean water tank, water inlet pipe, dissolved air pump, dissolved gas water pipe, gas flow meter and gas control valve, coagulation air flotation reaction system includes coagulation reaction column, adjustable stirring The solid-liquid separation system includes a solid-liquid separation column, a water level regulating valve, a clean water collection tank, a clean water collection pipe, a scum discharge pipe and a clean water discharge pipe. The utility model overcomes the problems of large floor space, high energy consumption, complicated management, blockage of fillers and large water loss.

Figure 201922371267

Description

混凝气浮实验系统Coagulation air flotation experiment system

技术领域technical field

本实用新型涉及环境工程水处理技术领域,尤其涉及一种混凝气浮实验系统。The utility model relates to the technical field of environmental engineering water treatment, in particular to a coagulation air flotation experiment system.

背景技术Background technique

随着经济的迅速发展,废水的超标排放导致的大面积水污染现象已经造成了生态环境的严重恶化,成为了制约社会经济发展的重要因素。为此,国家加强了对水环境的保护,同时严格规定污水排放标准。With the rapid development of the economy, the large-scale water pollution caused by the excessive discharge of wastewater has caused serious deterioration of the ecological environment and has become an important factor restricting social and economic development. To this end, the state has strengthened the protection of the water environment, and at the same time strictly stipulated the standards for sewage discharge.

对于中小水量的市政或工业水的深度处理,如中小城镇污水、石油、化工、造纸、皮革、印染、食品、淀粉的工业废水或工业园区污水等,新建水处理设施或升级改造的建设周期较长,影响项目建设或工业主体正常运行,而且在建设面积上比较紧张。For advanced treatment of municipal or industrial water with small and medium water volume, such as industrial wastewater from small and medium-sized cities and towns sewage, petroleum, chemical industry, papermaking, leather, printing and dyeing, food, starch, or industrial park sewage, the construction period for new water treatment facilities or upgrades is relatively short. It will affect the normal operation of the project construction or industrial main body, and the construction area is relatively tight.

对于景观河道水的处理,例如人工湿地、膜分离、混凝过滤和气浮等技术,然而,这些技术在保证处理效果的同时,占地面积大,能耗高,管理复杂,填料堵塞,损失水量大等缺点不能完全都避免。For the treatment of landscape river water, technologies such as constructed wetlands, membrane separation, coagulation filtration and air flotation, however, while ensuring the treatment effect, these technologies require a large area, high energy consumption, complex management, clogging of fillers, and water loss. Major disadvantages cannot be completely avoided.

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实验系统,以克服现有技术中的污水处理装置占地面积大、能耗高、管理复杂、填料堵塞和损失水量大等问题。The purpose of this utility model is to provide a coagulation-air flotation experiment system to overcome the problems of large footprint, high energy consumption, complex management, blockage of fillers and large water loss in the prior art sewage treatment devices.

为了解决上述技术问题,本实用新型提供了一种混凝气浮实验系统,包括加药混合系统、溶气气浮系统、混凝气浮反应系统和固液分离系统;In order to solve the above technical problems, the utility model provides a coagulation and air flotation experiment system, which includes a dosing mixing system, a dissolved air flotation system, a coagulation air flotation reaction system and a solid-liquid separation system;

所述加药混合系统包括PAM药箱、PAM计量泵、PAM加药管、PAC药箱、 PAC计量泵、PAC加药管、酸碱药箱、酸碱计量泵、酸碱加药管、污水箱、污水进入管、污水泵和污水管,所述PAM药箱通过所述PAM计量泵及PAM加药管与所述混凝气浮反应系统连接,所述污水泵的进水口通过所述污水进入管与所述污水箱连接,所述污水泵的出水口通过所述污水管与所述混凝气浮反应系统连接,所述PAC药箱通过所述PAC计量泵及PAC加药管与所述污水管连接,所述酸碱药箱通过所述酸碱计量泵及酸碱加药管与所述污水管连接;The dosing mixing system includes a PAM medicine box, a PAM metering pump, a PAM dosing pipe, a PAC medicine box, a PAC metering pump, a PAC dosing pipe, an acid-base medicine box, an acid-base metering pump, an acid-base dosing pipe, and sewage tank, sewage inlet pipe, sewage pump and sewage pipe, the PAM medicine box is connected with the coagulation air flotation reaction system through the PAM metering pump and the PAM dosing pipe, and the water inlet of the sewage pump passes through the sewage The inlet pipe is connected to the sewage tank, the water outlet of the sewage pump is connected to the coagulation air flotation reaction system through the sewage pipe, and the PAC medicine tank is connected to the water tank through the PAC metering pump and the PAC dosing pipe. The sewage pipe is connected, and the acid-base medicine box is connected with the sewage pipe through the acid-base metering pump and the acid-base dosing pipe;

所述溶气气浮系统包括清水箱、进水管、溶气泵、出溶气水管、气体流量计和气体控制阀,所述溶气泵的进水口通过进水管与所述清水箱连接,所述溶气泵的进气口通过管路与所述气体流量计连接,所述气体控制阀设在所述溶气泵与所述气体流量计之间的管路上,所述溶气泵的出水口通过所述出溶气水管与所述混凝气浮反应系统连接;The dissolved air flotation system includes a clean water tank, a water inlet pipe, a dissolved gas pump, a dissolved gas water pipe, a gas flow meter and a gas control valve. The water inlet of the dissolved gas pump is connected to the clean water tank through a water inlet pipe. The air inlet of the gas pump is connected to the gas flow meter through a pipeline, the gas control valve is arranged on the pipeline between the dissolved gas pump and the gas flow meter, and the water outlet of the dissolved gas pump passes through the outlet. The dissolved air water pipe is connected with the coagulation air flotation reaction system;

所述混凝气浮反应系统包括混凝反应柱、可调节搅拌器和连接管,所述可调节搅拌器设在所述混凝反应柱上,所述可调节搅拌器的搅拌部分位于所述混凝反应柱的内部,所述混凝反应柱通过所述连接管与所述固液分离系统连接;The coagulation-air flotation reaction system includes a coagulation reaction column, an adjustable stirrer and a connecting pipe, the adjustable agitator is arranged on the coagulation reaction column, and the stirring part of the adjustable agitator is located in the Inside the coagulation reaction column, the coagulation reaction column is connected with the solid-liquid separation system through the connecting pipe;

所述固液分离系统包括固液分离柱、水位调节阀、清水收集箱、清水收集管、浮渣排出管和清水排出管,所述水位调节阀设在所述固液分离柱的上端,所述清水收集箱和清水收集管均设在所述固液分离柱的内部,所述清水收集管的下端位于所述固液分离柱的下部,所述清水收集管的上端与所述清水收集箱的下端连接,所述浮渣排出管与所述固液分离柱上部的侧壁连接,所述清水收集箱通过所述清水排出管与所述清水箱连接。The solid-liquid separation system includes a solid-liquid separation column, a water level adjustment valve, a clean water collection tank, a clean water collection pipe, a scum discharge pipe and a clean water discharge pipe. The clean water collection tank and the clean water collection pipe are both arranged inside the solid-liquid separation column, the lower end of the clean water collection pipe is located at the lower part of the solid-liquid separation column, and the upper end of the clean water collection pipe is connected to the clean water collection tank. The lower end of the scum discharge pipe is connected to the side wall of the upper part of the solid-liquid separation column, and the clean water collection tank is connected to the clean water tank through the clean water discharge pipe.

优选的,所述PAM计量泵的进水口连接有PAM进药管,所述PAC计量泵的进水口连接有PAC进药管,所述酸碱计量泵的进水口连接有酸碱进药管。Preferably, the water inlet of the PAM metering pump is connected with a PAM medicine inlet pipe, the water inlet of the PAC metering pump is connected with a PAC medicine inlet pipe, and the water inlet of the acid-base metering pump is connected with an acid-base medicine inlet pipe.

优选的,所述PAM加药管通过两个支管与所述混凝反应柱连接,两个支管上分别设有PAM加药入口第一调节阀和PAM加药入口第二调节阀。Preferably, the PAM dosing pipe is connected to the coagulation reaction column through two branch pipes, and the two branch pipes are respectively provided with a first regulating valve for the PAM dosing inlet and a second regulating valve for the PAM dosing inlet.

优选的,所述污水进入管上设有调节阀,所述污水管上依次设有污水出口调节阀、污水流量计、污水出水管调节阀和污水管上调节阀。Preferably, the sewage inlet pipe is provided with a regulating valve, and the sewage pipe is sequentially provided with a sewage outlet regulating valve, a sewage flow meter, a sewage outlet pipe regulating valve and a sewage pipe upper regulating valve.

优选的,所述进水管上设有进水控制阀和真空表,所述出溶气水管上依次设有水量调节阀、溶气水流量计、压力表、水流调节阀和溶气水取样阀。Preferably, the water inlet pipe is provided with a water inlet control valve and a vacuum gauge, and the dissolved gas water pipe is sequentially provided with a water volume regulating valve, a dissolved gas water flowmeter, a pressure gauge, a water flow regulating valve and a dissolved gas water sampling valve .

优选的,所述出溶气水管通过两个支管与所述混凝反应柱连接,两个支管上分别设有溶气水入口第一调节阀和溶气水入口第二调节阀。Preferably, the dissolved gas water pipe is connected to the coagulation reaction column through two branch pipes, and the two branch pipes are respectively provided with a first regulating valve of the dissolved gas water inlet and a second regulating valve of the dissolved gas water inlet.

优选的,所述清水箱的上部设有清水箱溢流管。Preferably, the upper part of the clean water tank is provided with a clean water tank overflow pipe.

优选的,所述混凝反应柱的侧壁设有多个高度不同的取样阀。Preferably, the side wall of the coagulation reaction column is provided with a plurality of sampling valves with different heights.

优选的,所述固液分离柱的侧壁设有多个高度不同的取样阀。Preferably, the side wall of the solid-liquid separation column is provided with a plurality of sampling valves with different heights.

本实用新型的混凝气浮实验系统包括加药混合系统、溶气气浮系统、混凝气浮反应系统和固液分离系统组成,通过设置独立的混凝气浮反应系统和固液分离系统来实现混凝气浮分离过程的优化,同时,在排浮渣方式上采用水位调节控制实现变水位排渣方式,简易便捷,整套设备占地小,投资少,效率高,更便于对多样化污水进行混凝和气浮处理方式的研究和探讨。The coagulation-air flotation experiment system of the utility model is composed of a dosing mixing system, a dissolved-air flotation system, a coagulation-air flotation reaction system and a solid-liquid separation system. To achieve the optimization of the coagulation-air flotation separation process, at the same time, the water level adjustment control is used in the scum discharge method to realize the variable water level slag discharge method, which is simple and convenient, the whole set of equipment occupies a small area, low investment, high efficiency, and is more convenient for diversification. Research and discussion on coagulation and air flotation treatment of sewage.

附图说明Description of drawings

图1为本实用新型实施例的混凝气浮实验系统的结构示意图。FIG. 1 is a schematic structural diagram of a coagulation-air flotation experiment system according to an embodiment of the present invention.

图中,1:PAM药箱;2:PAM进药管;3:PAM计量泵;4:PAM加药管;5:PAM加药入口第一调节阀;6:PAM加药入口第二调节阀;7:PAC药箱;8: PAC进药管;9:PAC计量泵;10:PAC加药管;11:酸碱药箱;12:酸碱进药管;13:酸碱计量泵;14:酸碱加药管;15:污水泵;16:污水进入管;17:污水出口调节阀;18:污水流量计;19:污水出水管调节阀;20:污水管;21:污水管上调节阀;22:污水箱;23:混凝反应柱;24:可调节搅拌器;25:取样阀;26:清水箱;27:溶气泵;28:进水管;29:进水控制阀;30:真空表; 31:气体流量计;32:气体控制阀;33:水量调节阀;34:溶气水流量计;35:压力表;36:水流调节阀;37:溶气水取样阀;38:出溶气水管;39:溶气水入口第一调节阀;40:溶气水入口第二调节阀;41:连接管;42:固液分离柱; 43:水位调节阀;44:请水收集管;45:清水收集箱;46:清水排出管;47:浮渣排出管;48:清水箱溢流管。In the figure, 1: PAM medicine box; 2: PAM medicine inlet pipe; 3: PAM metering pump; 4: PAM medicine addition pipe; 5: PAM medicine inlet first regulating valve; 6: PAM medicine inlet second regulating valve ;7: PAC medicine box; 8: PAC medicine inlet pipe; 9: PAC metering pump; 10: PAC medicine addition pipe; 11: acid-base medicine box; 12: acid-base medicine inlet pipe; 13: acid-base metering pump; 14 : Acid-base dosing pipe; 15: Sewage pump; 16: Sewage inlet pipe; 17: Sewage outlet regulating valve; 18: Sewage flow meter; 19: Sewage outlet pipe regulating valve; 20: Sewage pipe; 21: Adjustment on the sewage pipe valve; 22: sewage tank; 23: coagulation reaction column; 24: adjustable stirrer; 25: sampling valve; 26: clean water tank; 27: dissolved air pump; 28: water inlet pipe; 29: water inlet control valve; 30: Vacuum gauge; 31: Gas flow meter; 32: Gas control valve; 33: Water volume regulating valve; 34: Dissolved gas water flow meter; 35: Pressure gauge; 36: Water flow regulating valve; 37: Dissolved gas water sampling valve; 38: Dissolved gas water pipe; 39: Dissolved gas water inlet first regulating valve; 40: Dissolved gas water inlet second regulating valve; 41: Connecting pipe; 42: Solid-liquid separation column; 43: Water level regulating valve; 44: Please collect water pipe; 45: clear water collection tank; 46: clear water discharge pipe; 47: scum discharge pipe; 48: clear water tank overflow 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 embodiments of the present utility model will be described in further detail below with reference to the accompanying drawings and examples. The following examples are used to illustrate the present invention, but cannot be used to limit the scope of the present invention.

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 invention, it should be noted that the terms "center", "longitudinal", "horizontal", "upper", "lower", "front", "rear", "left", "right", The orientations or positional relationships indicated by "vertical", "horizontal", "top", "bottom", "inside", "outside", etc. are based on the orientations or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present utility. The novel and simplified description does not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operate in a particular orientation, and therefore should not be construed as limiting the invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and should not be construed to indicate or imply 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 invention, it should be noted that, unless otherwise expressly specified and limited, the terms "installed", "connected" and "connected" should be understood in a broad sense, for example, it may be a fixed connection or a connectable connection. Detachable connection, or integral connection; may be mechanical connection or electrical connection; may be direct connection, or indirect connection through an intermediate medium, or internal communication between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific situations. In addition, in the description of the present invention, unless otherwise specified, the meaning of "plurality" is two or more.

如图1所示,本实施例的混凝气浮实验系统包括:加药混合系统、溶气气浮系统、混凝气浮反应系统和固液分离系统。As shown in FIG. 1 , the coagulation-air flotation experiment system of this embodiment includes: a dosing and mixing system, a dissolved-air flotation system, a coagulation-air flotation reaction system, and a solid-liquid separation system.

加药混合系统包括:PAM药箱1、PAM计量泵3、PAM加药管4、PAC药箱7、 PAC计量泵9、PAC加药管10、酸碱药箱11、酸碱计量泵13、酸碱加药管14、污水箱22、污水进入管16、污水泵15和污水管20,PAM药箱通过PAM计量泵3及PAM 加药管4与混凝气浮反应系统连接,污水泵15的进水口通过污水进入管16与污水箱22连接,污水泵15的出水口通过污水管20与混凝气浮反应系统连接,PAC药箱 7通过PAC计量泵及PAC加药管10与污水管20连接,酸碱药箱11通过酸碱计量泵 13及酸碱加药管14与污水管20连接。PAM计量泵3的进水口连接有PAM进药管2, PAC计量泵9的进水口连接有PAC进药管8,酸碱计量泵13的进水口连接有酸碱进药管12。PAM加药管4通过两个支管与混凝反应柱23连接,两个支管上分别设有 PAM加药入口第一调节阀5和PAM加药入口第二调节阀6。污水进入管16上设有调节阀,污水管20上依次设有污水出口调节阀17、污水流量计18、污水出水管调节阀19和污水管上调节阀21。The dosing mixing system includes: PAM medicine box 1, PAM metering pump 3, PAM dosing pipe 4, PAC medicine box 7, PAC metering pump 9, PAC dosing pipe 10, acid-base medicine box 11, acid-base metering pump 13, Acid-base dosing pipe 14, sewage tank 22, sewage inlet pipe 16, sewage pump 15 and sewage pipe 20, PAM medicine tank is connected with coagulation air flotation reaction system through PAM metering pump 3 and PAM dosing pipe 4, sewage pump 15 The water inlet of the PAC is connected to the sewage tank 22 through the sewage inlet pipe 16, the water outlet of the sewage pump 15 is connected to the coagulation air flotation reaction system through the sewage pipe 20, and the PAC medicine box 7 is connected to the sewage pipe through the PAC metering pump and the PAC dosing pipe 10. 20 is connected, and the acid-base medicine tank 11 is connected to the sewage pipe 20 through the acid-base metering pump 13 and the acid-base dosing pipe 14 . The water inlet of the PAM metering pump 3 is connected with the PAM medicine inlet pipe 2 , the water inlet of the PAC metering pump 9 is connected with the PAC medicine inlet pipe 8 , and the water inlet of the acid-base metering pump 13 is connected with the acid-base medicine inlet pipe 12 . The PAM dosing pipe 4 is connected to the coagulation reaction column 23 through two branch pipes, and the two branch pipes are respectively provided with a PAM dosing inlet first regulating valve 5 and a PAM dosing inlet second regulating valve 6 . The sewage inlet pipe 16 is provided with a regulating valve, and the sewage pipe 20 is sequentially provided with a sewage outlet regulating valve 17, a sewage flow meter 18, a sewage outlet pipe regulating valve 19 and a sewage pipe upper regulating valve 21.

打开污水进入管16,污水由污水泵15从污水箱22中吸入,通过流量计18和阀门17控制流量进入污水管20中,同时混凝剂、酸或碱调节剂分别通过计量泵9 和13的控制吸入加药管10和14中,再一同进入污水管20,使药液与污水混合,混合后经过调节阀21进入混凝气浮系统内,同时助凝剂PAM由计量泵3吸入PAM 加药管4中,再通过PAM加药入口第一调节阀5和PAM加药入口第二调节阀6的控制加入到混凝气浮系统。混凝剂PAC、pH调节剂通过计量泵控制加药量后输出到污水管中,使药液与污水混合,污水出水由污水管上的流量计和调节阀控制,污水管中与药液混合后的污水通过污水管上调节阀进入混凝气浮柱的底端,助凝剂PAM计量泵和加药调节阀控制分别加入到混凝气浮系统内两个加药点。Open the sewage inlet pipe 16, the sewage is sucked from the sewage tank 22 by the sewage pump 15, and the flow is controlled by the flow meter 18 and the valve 17 to enter the sewage pipe 20, and the coagulant, acid or alkali regulator are respectively passed through the metering pumps 9 and 13. The controlled suction is inhaled into the dosing pipes 10 and 14, and then enters the sewage pipe 20 together, so that the medicinal liquid is mixed with the sewage, and after mixing, it enters the coagulation air flotation system through the regulating valve 21, and the coagulant PAM is sucked into the PAM by the metering pump 3. In the dosing pipe 4, it is added to the coagulation air flotation system through the control of the first regulating valve 5 of the PAM dosing inlet and the second regulating valve 6 of the PAM dosing inlet. The coagulant PAC and pH adjuster are controlled by the metering pump and then output to the sewage pipe, so that the liquid medicine is mixed with the sewage. The last sewage enters the bottom end of the coagulation air flotation column through the regulating valve on the sewage pipe, and the coagulant PAM metering pump and the dosing regulating valve are controlled to be added to the two dosing points in the coagulation air flotation system respectively.

溶气气浮系统包括:清水箱26、进水管28、溶气泵27、出溶气水管38、气体流量计31和气体控制阀32,溶气泵27的进水口通过进水管28与清水箱26连接,溶气泵27的进气口通过管路与气体流量计31连接,气体控制阀32设在溶气泵27 与气体流量计31之间的管路上,溶气泵27的出水口通过出溶气水管38与混凝气浮反应系统连接。进水管28上设有进水控制阀29和真空表30,出溶气水管38上依次设有水量调节阀33、溶气水流量计34、压力表35、水流调节阀36和溶气水取样阀37。出溶气水管38通过两个支管与混凝反应柱23连接,两个支管上分别设有溶气水入口第一调节阀39和溶气水入口第二调节阀40。清水箱26的上部设有清水箱溢流管48。The dissolved air flotation system includes: a clean water tank 26, a water inlet pipe 28, a dissolved gas pump 27, a dissolved gas water pipe 38, a gas flow meter 31 and a gas control valve 32, and the water inlet of the dissolved gas pump 27 is connected to the clean water tank 26 through the water inlet pipe 28 , the air inlet of the dissolved gas pump 27 is connected with the gas flow meter 31 through the pipeline, the gas control valve 32 is arranged on the pipeline between the dissolved gas pump 27 and the gas flow meter 31, and the water outlet of the dissolved gas pump 27 passes through the dissolved gas water pipe 38 Connect with the coagulation air flotation reaction system. The water inlet pipe 28 is provided with a water inlet control valve 29 and a vacuum gauge 30, and the dissolved gas water pipe 38 is sequentially provided with a water volume regulating valve 33, a dissolved gas water flowmeter 34, a pressure gauge 35, a water flow regulating valve 36 and a dissolved gas water sampling valve 37. The dissolved gas water pipe 38 is connected to the coagulation reaction column 23 through two branch pipes, and the two branch pipes are respectively provided with a dissolved gas water inlet first regulating valve 39 and a dissolved gas water inlet second regulating valve 40 . The upper part of the clean water tank 26 is provided with a clean water tank overflow pipe 48 .

打开进水控制阀29,开启溶气泵27,将清水箱26中的水吸入泵体,通过进水控制阀29和真空表30控制,同时溶气泵通过气体流量计31和气体控制阀32控制吸入空气,空气经溶气泵被反复切割后,压力维持在0.3-0.5Mpa范围内,压力由压力表35显示,通过溶气水流量计34控制加入量,打开溶气水取样阀37观察溶气效果后关闭,由出溶气水管38输送至混凝气浮系统的中部和下部,通过溶气和释放系统在水中产生大量的微细气泡,使其黏附于废水中密度与水接近的固体或液体微粒上,造成整体密度小于水的状态,并依靠浮力使其上升至水面,从而达到固—液或液—液分离的目的。溶气泵进水管连接清水箱底端,通过进水控制阀门控制流量,溶气泵吸入管路上与其平行位置上设有空气进气嘴,通过进气流量计和调节阀定量空气,空气被溶气泵反复切割后,使气体分散溶入水中,压力维持在0.2-0.3Mpa范围内,溶气水出水管连接溶气水流量计、水流调节阀、压力表、溶气水取样阀,出溶气水后通过出溶气水入口第一调节阀或溶气水入口第二调节阀将溶气水通入混凝气浮反应柱内。Open the water inlet control valve 29, open the dissolved air pump 27, suck the water in the clean water tank 26 into the pump body, and control it through the water inlet control valve 29 and the vacuum gauge 30, while the dissolved air pump controls the suction through the gas flow meter 31 and the gas control valve 32. Air, after the air is repeatedly cut by the dissolved air pump, the pressure is maintained in the range of 0.3-0.5Mpa, the pressure is displayed by the pressure gauge 35, the added amount is controlled by the dissolved air water flowmeter 34, and the dissolved air water sampling valve 37 is opened to observe the dissolved air effect. After closing, it is transported to the middle and lower parts of the coagulation and air flotation system by the dissolved gas water pipe 38, and a large number of fine bubbles are generated in the water through the dissolved gas and release system, so that they adhere to the solid or liquid particles in the wastewater whose density is close to that of water. , resulting in a state where the overall density is less than that of water, and relying on buoyancy to make it rise to the water surface, so as to achieve the purpose of solid-liquid or liquid-liquid separation. The water inlet pipe of the dissolved air pump is connected to the bottom of the clean water tank, and the flow rate is controlled by the water inlet control valve. There is an air intake nozzle on the inhalation pipeline of the dissolved air pump at a position parallel to it. The air is quantified by the air inlet flowmeter and the regulating valve, and the air is repeatedly cut by the dissolved air pump. Then, disperse the gas and dissolve it into the water, and keep the pressure in the range of 0.2-0.3Mpa. The dissolved gas water outlet pipe is connected to the dissolved gas water flowmeter, water flow regulating valve, pressure gauge, and dissolved gas water sampling valve. The dissolved gas water inlet first regulating valve or the dissolved gas water inlet second regulating valve passes the dissolved gas water into the coagulation air flotation reaction column.

混凝气浮反应系统包括:混凝反应柱23、可调节搅拌器24和连接管41,可调节搅拌器24设在混凝反应柱23上,可调节搅拌器24的搅拌部分位于混凝反应柱23的内部,混凝反应柱23通过连接管41与固液分离系统连接。混凝反应柱23 的侧壁设有多个高度不同的取样阀25。The coagulation air flotation reaction system includes: a coagulation reaction column 23, an adjustable agitator 24 and a connecting pipe 41, the adjustable agitator 24 is arranged on the coagulation reaction column 23, and the stirring part of the adjustable agitator 24 is located in the coagulation reaction Inside the column 23 , the coagulation reaction column 23 is connected to the solid-liquid separation system through the connecting pipe 41 . The side wall of the coagulation reaction column 23 is provided with a plurality of sampling valves 25 with different heights.

启动搅拌机24,打开阀门5和6、调节阀21、溶气水进入阀,PAC混合液和PAM 药液分别从反应柱底部和中部通过阀门进入,溶气水同时由控制阀控制从柱体底部和中部进入,此时加药混合液与溶气水在搅拌器24的作用下开始混合反应,通过搅拌杆和搅拌叶片的作用,使加入的药剂、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,开启取样阀25可观察反应柱内上中下位置的反应状态和效果,反应后的混合液在柱体上部通过连接管41与阀流进固液分离系统中进行固液分离。加药混合后的混合液经污水管与阀从混凝反应柱体下端通入,入口上方同时通入助凝剂PAM,加药混合水在搅拌器的作用下进行充分混合,此时溶气水从混凝反应柱底端通过2个入口阀门控制分别加入系统内,在搅拌机器带动下通过搅拌杆和搅拌叶片的作用,使加入的药剂、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,通过连接管与阀流进固液分离系统进行固液分离;混凝气浮反应系统内混合液的混凝絮凝反应、气浮反应的方式,可通过进水阀门分别控制,由上中下三个取样阀观察反应状态和效果。Start the mixer 24, open the valves 5 and 6, the regulating valve 21, the dissolved gas water inlet valve, the PAC mixture and the PAM liquid enter through the valve from the bottom and middle of the reaction column respectively, and the dissolved gas water is controlled by the control valve at the same time from the bottom of the column. And the middle part enters, at this time, the mixed liquid and the dissolved gas and water start to mix and react under the action of the stirrer 24. Through the action of the stirring rod and the stirring blade, the added medicine, water and gas can be added more quickly, evenly and effectively. Mixing to form a copolymer complex of larger bubbles and flocs, open the sampling valve 25 to observe the reaction state and effect of the upper, middle and lower positions in the reaction column, and the mixed liquid after the reaction flows into the upper part of the column through the connecting pipe 41 and the valve. Solid-liquid separation is performed in a solid-liquid separation system. The mixed liquid after dosing and mixing is introduced from the lower end of the coagulation reaction cylinder through the sewage pipe and valve, and the coagulation aid PAM is simultaneously introduced above the inlet, and the mixed water is fully mixed under the action of the agitator. Water is added into the system from the bottom of the coagulation reaction column through two inlet valves, and driven by the stirring machine, the stirring rod and the stirring blade make the added medicine, water and gas more quickly, uniformly and effectively mixed. , to form a copolymer complex of larger bubbles and flocs, and flow into the solid-liquid separation system through the connecting pipe and valve for solid-liquid separation; It can be controlled separately by the water inlet valve, and the reaction state and effect can be observed by the upper, middle and lower sampling valves.

固液分离系统包括:固液分离柱42、水位调节阀43、清水收集箱45、清水收集管44、浮渣排出管47和清水排出管46,水位调节阀43设在固液分离柱42的上端,清水收集箱45和清水收集管44均设在固液分离柱42的内部,清水收集管 44的下端位于固液分离柱42的下部,清水收集管44的上端与清水收集箱45的下端连接,浮渣排出管47与固液分离柱42上部的侧壁连接,清水收集箱45通过清水排出管46与清水箱26连接。固液分离柱42的侧壁设有多个高度不同的取样阀。The solid-liquid separation system includes: a solid-liquid separation column 42, a water level adjustment valve 43, a clean water collection tank 45, a clean water collection pipe 44, a scum discharge pipe 47 and a clean water discharge pipe 46, and the water level adjustment valve 43 is provided in the solid-liquid separation column 42. On the upper end, the clean water collection tank 45 and the clean water collection pipe 44 are all arranged inside the solid-liquid separation column 42, the lower end of the clean water collection pipe 44 is located at the lower part of the solid-liquid separation column 42, the upper end of the clean water collection pipe 44 and the lower end of the clean water collection tank 45. The scum discharge pipe 47 is connected to the upper side wall of the solid-liquid separation column 42, and the clean water collection tank 45 is connected to the clean water tank 26 through the clean water discharge pipe 46. The side wall of the solid-liquid separation column 42 is provided with a plurality of sampling valves with different heights.

打开连接管41上的阀,来水通过连接管41在固液分离柱42的上端位置进水,混合液中的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,该复合体密度与水的密度差较大会自动上升到分离柱内液面处,形成浮渣层,关闭水位调节阀43,液面上升后浮渣通过浮渣排出管47排出;而分离后的净水被收集到清水收集箱45中,经过清水排出管46排到清水箱26内,完成固液分离操作。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液通过连接溢流进入固液分离区内,连接管在固液分离柱上端位置进水,混合液进入固液分离柱后,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,会自动上升到分离柱液面处,形成浮渣层实现快速的固液分离,浮渣通过关闭清水收集箱上方的水位调节阀后,液面上升使浮渣经过浮渣排出管排出;分离的净水从分离柱下端的清水收集管收集到上端的清水收集箱内,再通过清水排出管导入清水箱中。Open the valve on the connecting pipe 41, and the incoming water enters the upper end of the solid-liquid separation column 42 through the connecting pipe 41. The density of the co-polymer complex of bubbles and flocs in the mixed liquid is relatively different from that of water, and the particle size is larger. It is much larger than the particles in the original sewage, and the density difference between the composite body and the water is large, and it will automatically rise to the liquid level in the separation column to form a scum layer, close the water level regulating valve 43, and the scum will pass through the scum after the liquid level rises. The discharge pipe 47 is discharged; and the separated clean water is collected in the clean water collection tank 45, and discharged into the clean water tank 26 through the clean water discharge pipe 46 to complete the solid-liquid separation operation. After the mixing and flocculation of the liquid medicine is completed, the mixed liquid that forms a copolymer complex of larger particle size bubbles and flocs enters the solid-liquid separation zone through the connection overflow. The connecting pipe enters the upper end of the solid-liquid separation column, and the mixed liquid enters the solid-liquid separation column. After the liquid separation column, the density of the copolymer complex of larger bubbles and flocs formed is larger than the density of water, and the particle size is much larger than the particles in the original sewage, which will automatically rise to the liquid surface of the separation column to form scum. The layer realizes rapid solid-liquid separation. After the scum closes the water level control valve above the clean water collection tank, the liquid level rises and the scum is discharged through the scum discharge pipe; the separated clean water is collected from the clean water collection pipe at the lower end of the separation column to the upper end. into the clean water collection tank, and then lead it into the clean water tank through the clean water discharge pipe.

本实用新型的混凝气浮实验系统包括加药混合系统、溶气气浮系统、混凝气浮反应系统和固液分离系统组成,通过设置独立的混凝气浮反应系统和固液分离系统来实现混凝气浮分离过程的优化,同时,在排浮渣方式上采用水位调节控制实现变水位排渣方式,简易便捷,整套设备占地小,投资少,效率高,更便于对多样化污水进行混凝和气浮处理方式的研究和探讨。The coagulation-air flotation experiment system of the utility model is composed of a dosing mixing system, a dissolved-air flotation system, a coagulation-air flotation reaction system and a solid-liquid separation system. To achieve the optimization of the coagulation-air flotation separation process, at the same time, the water level adjustment control is used in the scum discharge method to realize the variable water level slag discharge method, which is simple and convenient, the whole set of equipment occupies a small area, low investment, high efficiency, and is more convenient for diversification. Research and discussion on coagulation and air flotation treatment of sewage.

本实用新型的混凝气浮实验系统采用了混凝气浮工艺,充分运用了混凝气浮的基本原理,缩短反应分离时间,提高上浮絮渣的稳定性与上浮能力,出水通过水位调节控制分离柱被的排浮渣,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,大大提高了分离效率与稳定性。由于混凝气浮工艺适用于各种水质且处理效果好,因此本实用新型的混凝气浮实验系统可以有效地去除废水中难以沉淀的轻浮絮体,处理能力大、效率高、占地少、适用范围广。同时,本实用新型的混凝气浮实验系统可以预先设计多种方式,通过控制开闭加药系统阀门或气浮系统出溶气水管路阀门,可研究混凝或气浮单独作用的效果,使用时根据相应的处理状态和效果选择相应的方式即可。将各种水处理设施集成在一个组合中后可以便于运输、减小占地面积,降低溶气能耗,提高处理效率,简化工艺流程。另外本实用新型的混凝气浮实验系统不需要建造工期,可以立即投入使用,整体投资低。The coagulation-air flotation experiment system of the utility model adopts the coagulation-air flotation process, fully utilizes the basic principle of coagulation-air flotation, shortens the reaction separation time, improves the stability and floating capacity of the floating flocculation residue, and the effluent is controlled by water level adjustment. The scum is discharged from the separation column to realize the concentration and dehydration of the scum in the solid-liquid separation zone, which can further reduce the moisture content of the floc and greatly improve the separation efficiency and stability. Since the coagulation-air flotation process is suitable for various water quality and has good treatment effect, the coagulation-air flotation experimental system of the present invention can effectively remove the light flocs that are difficult to settle in the wastewater, and has large processing capacity, high efficiency and small footprint. ,Wide range of applications. At the same time, the coagulation and air flotation experimental system of the present utility model can be designed in various ways in advance. By controlling the opening and closing of the valve of the dosing system or the valve of the dissolved gas and water pipeline of the air flotation system, the effect of coagulation or air flotation alone can be studied. When using, you can select the corresponding method according to the corresponding processing state and effect. Integrating various water treatment facilities into one combination can facilitate transportation, reduce floor space, reduce dissolved gas energy consumption, improve treatment efficiency, and simplify process flow. In addition, the coagulation-air flotation experiment system of the present invention does not require a construction period, can be put into use immediately, and the overall investment is low.

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 present invention are presented for purposes of illustration and description, and are not intended to be exhaustive or to limit the invention to the form disclosed. Many modifications and variations will be apparent to those of ordinary skill in the art. The embodiment was chosen and described in order to better explain the principles of the invention and the practical application, and to enable others of ordinary skill in the art to understand the invention for the design of various embodiments with various modifications as are suited to the particular use.

Claims (9)

1.一种混凝气浮实验系统,其特征在于,包括加药混合系统、溶气气浮系统、混凝气浮反应系统和固液分离系统;1. a coagulation air flotation experiment system, is characterized in that, comprises dosing mixing system, dissolved air flotation system, coagulation air flotation reaction system and solid-liquid separation system; 所述加药混合系统包括PAM药箱(1)、PAM计量泵(3)、PAM加药管(4)、PAC药箱(7)、PAC计量泵(9)、PAC加药管(10)、酸碱药箱(11)、酸碱计量泵(13)、酸碱加药管(14)、污水箱(22)、污水进入管(16)、污水泵(15)和污水管(20),所述PAM药箱通过所述PAM计量泵(3)及PAM加药管(4)与所述混凝气浮反应系统连接,所述污水泵(15)的进水口通过所述污水进入管(16)与所述污水箱(22)连接,所述污水泵(15)的出水口通过所述污水管(20)与所述混凝气浮反应系统连接,所述PAC药箱(7)通过所述PAC计量泵及PAC加药管(10)与所述污水管(20)连接,所述酸碱药箱(11)通过所述酸碱计量泵(13)及酸碱加药管(14)与所述污水管(20)连接;The medicine dosing and mixing system includes a PAM medicine box (1), a PAM metering pump (3), a PAM medicine addition pipe (4), a PAC medicine box (7), a PAC metering pump (9), and a PAC medicine addition pipe (10) , acid-base medicine tank (11), acid-base metering pump (13), acid-base dosing pipe (14), sewage tank (22), sewage inlet pipe (16), sewage pump (15) and sewage pipe (20) , the PAM medicine box is connected with the coagulation air flotation reaction system through the PAM metering pump (3) and the PAM dosing pipe (4), and the water inlet of the sewage pump (15) passes through the sewage inlet pipe (16) is connected to the sewage tank (22), the water outlet of the sewage pump (15) is connected to the coagulation air flotation reaction system through the sewage pipe (20), and the PAC medicine tank (7) The PAC metering pump and the PAC dosing pipe (10) are connected to the sewage pipe (20), and the acid-base medicine tank (11) is connected to the acid-base metering pump (13) and the acid-base dosing pipe ( 14) Connect with the sewage pipe (20); 所述溶气气浮系统包括清水箱(26)、进水管(28)、溶气泵(27)、出溶气水管(38)、气体流量计(31)和气体控制阀(32),所述溶气泵(27)的进水口通过进水管(28)与所述清水箱(26)连接,所述溶气泵(27)的进气口通过管路与所述气体流量计(31)连接,所述气体控制阀(32)设在所述溶气泵(27)与所述气体流量计(31)之间的管路上,所述溶气泵(27)的出水口通过所述出溶气水管(38)与所述混凝气浮反应系统连接;The dissolved air flotation system comprises a clean water tank (26), a water inlet pipe (28), a dissolved gas pump (27), a dissolved gas water pipe (38), a gas flow meter (31) and a gas control valve (32). The water inlet of the dissolved air pump (27) is connected to the clean water tank (26) through a water inlet pipe (28), and the air inlet of the dissolved air pump (27) is connected to the gas flow meter (31) through a pipeline, so The gas control valve (32) is arranged on the pipeline between the dissolved gas pump (27) and the gas flow meter (31), and the water outlet of the dissolved gas pump (27) passes through the dissolved gas water pipe (38). ) is connected with the coagulation air flotation reaction system; 所述混凝气浮反应系统包括混凝反应柱(23)、可调节搅拌器(24)和连接管(41),所述可调节搅拌器(24)设在所述混凝反应柱(23)上,所述可调节搅拌器(24)的搅拌部分位于所述混凝反应柱(23)的内部,所述混凝反应柱(23)通过所述连接管(41)与所述固液分离系统连接;The coagulation-air flotation reaction system comprises a coagulation reaction column (23), an adjustable stirrer (24) and a connecting pipe (41), and the adjustable agitator (24) is arranged on the coagulation reaction column (23) ), the stirring part of the adjustable stirrer (24) is located inside the coagulation reaction column (23), and the coagulation reaction column (23) communicates with the solid-liquid through the connecting pipe (41). separate system connections; 所述固液分离系统包括固液分离柱(42)、水位调节阀(43)、清水收集箱(45)、清水收集管(44)、浮渣排出管(47)和清水排出管(46),所述水位调节阀(43)设在所述固液分离柱(42)的上端,所述清水收集箱(45)和清水收集管(44)均设在所述固液分离柱(42)的内部,所述清水收集管(44)的下端位于所述固液分离柱(42)的下部,所述清水收集管(44)的上端与所述清水收集箱(45)的下端连接,所述浮渣排出管(47)与所述固液分离柱(42) 上部的侧壁连接,所述清水收集箱(45)通过所述清水排出管(46)与所述清水箱(26)连接。The solid-liquid separation system includes a solid-liquid separation column (42), a water level regulating valve (43), a clean water collection tank (45), a clean water collection pipe (44), a scum discharge pipe (47) and a clean water discharge pipe (46) , the water level regulating valve (43) is arranged on the upper end of the solid-liquid separation column (42), and the clean water collection tank (45) and the clean water collection pipe (44) are both arranged on the solid-liquid separation column (42) Inside, the lower end of the clean water collection pipe (44) is located at the lower part of the solid-liquid separation column (42), and the upper end of the clean water collection pipe (44) is connected with the lower end of the clean water collection tank (45), so The scum discharge pipe (47) is connected to the upper side wall of the solid-liquid separation column (42), and the clean water collection tank (45) is connected to the clean water tank (26) through the clean water discharge pipe (46) . 2.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述PAM计量泵(3)的进水口连接有PAM进药管(2),所述PAC计量泵(9)的进水口连接有PAC进药管(8),所述酸碱计量泵(13)的进水口连接有酸碱进药管(12)。2. The coagulation-air flotation experiment system according to claim 1, wherein the water inlet of the PAM metering pump (3) is connected with the PAM medicine inlet pipe (2), and the PAC metering pump (9) The water inlet is connected with a PAC medicine inlet pipe (8), and the water inlet of the acid-base metering pump (13) is connected with an acid-base medicine inlet pipe (12). 3.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述PAM加药管(4)通过两个支管与所述混凝反应柱(23)连接,两个支管上分别设有PAM加药入口第一调节阀(5)和PAM加药入口第二调节阀(6)。3. The coagulation air flotation experiment system according to claim 1, wherein the PAM dosing pipe (4) is connected to the coagulation reaction column (23) through two branch pipes, and the two branch pipes are respectively A first regulating valve (5) for the PAM dosing inlet and a second regulating valve (6) for the PAM dosing inlet are provided. 4.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述污水进入管(16)上设有调节阀,所述污水管(20)上依次设有污水出口调节阀(17)、污水流量计(18)、污水出水管调节阀(19)和污水管上调节阀(21)。4. The coagulation-air flotation experiment system according to claim 1, wherein the sewage inlet pipe (16) is provided with a regulating valve, and the sewage pipe (20) is sequentially provided with a sewage outlet regulating valve ( 17), sewage flow meter (18), sewage outlet pipe regulating valve (19) and sewage pipe upper regulating valve (21). 5.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述进水管(28)上设有进水控制阀(29)和真空表(30),所述出溶气水管(38)上依次设有水量调节阀(33)、溶气水流量计(34)、压力表(35)、水流调节阀(36)和溶气水取样阀(37)。5. The coagulation-air flotation experiment system according to claim 1, wherein the water inlet pipe (28) is provided with a water inlet control valve (29) and a vacuum gauge (30), and the dissolved gas water pipe is provided with a water inlet control valve (29) and a vacuum gauge (30). (38) are sequentially provided with a water volume regulating valve (33), a dissolved gas water flowmeter (34), a pressure gauge (35), a water flow regulating valve (36) and a dissolved gas water sampling valve (37). 6.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述出溶气水管(38)通过两个支管与所述混凝反应柱(23)连接,两个支管上分别设有溶气水入口第一调节阀(39)和溶气水入口第二调节阀(40)。6. The coagulation air flotation experiment system according to claim 1, wherein the dissolved gas water pipe (38) is connected to the coagulation reaction column (23) through two branch pipes, and the two branch pipes are respectively connected to the coagulation reaction column (23). A first regulating valve (39) for the dissolved air and water inlet and a second regulating valve (40) for the dissolved gas and water inlet are provided. 7.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述清水箱(26)的上部设有清水箱溢流管(48)。7. The coagulation-air flotation experiment system according to claim 1, characterized in that, a clean water tank overflow pipe (48) is provided on the upper part of the clean water tank (26). 8.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述混凝反应柱(23)的侧壁设有多个高度不同的取样阀(25)。8. The coagulation-air flotation experiment system according to claim 1, characterized in that, a plurality of sampling valves (25) with different heights are provided on the side wall of the coagulation reaction column (23). 9.根据权利要求1所述的混凝气浮实验系统,其特征在于,所述固液分离柱(42)的侧壁设有多个高度不同的取样阀。9 . The coagulation-air flotation experiment system according to claim 1 , wherein a plurality of sampling valves with different heights are arranged on the side wall of the solid-liquid separation column ( 42 ). 10 .
CN201922371267.2U 2019-12-26 2019-12-26 Coagulation air flotation experiment system Expired - Fee Related CN211620175U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113045024A (en) * 2019-12-26 2021-06-29 大连交通大学 Coagulation and air floatation integrated experimental device
CN113041659A (en) * 2021-04-30 2021-06-29 河南卷烟工业烟草薄片有限公司 Air supporting dross defoaming processing apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113045024A (en) * 2019-12-26 2021-06-29 大连交通大学 Coagulation and air floatation integrated experimental device
CN113041659A (en) * 2021-04-30 2021-06-29 河南卷烟工业烟草薄片有限公司 Air supporting dross defoaming processing apparatus

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