CN111943329A - High-chlorine high-ammonia nitrogen wastewater treatment device with three-dimensional electrode - Google Patents

High-chlorine high-ammonia nitrogen wastewater treatment device with three-dimensional electrode Download PDF

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CN111943329A
CN111943329A CN202010873397.0A CN202010873397A CN111943329A CN 111943329 A CN111943329 A CN 111943329A CN 202010873397 A CN202010873397 A CN 202010873397A CN 111943329 A CN111943329 A CN 111943329A
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electrolytic cell
cathode
plate
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electrode
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叶芳芳
李长刚
张帅
李阳
杨振兴
谢文玉
李德豪
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Guangdong University of Petrochemical Technology
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4602Treatment of water, waste water, or sewage by electrochemical methods for prevention or elimination of deposits
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F2201/46Apparatus for electrochemical processes
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    • C02F2201/4619Supplying gas to the electrolyte

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Abstract

本发明提供带三维电极的高氯高氨氮废水处理装置,包括电解池、阳极电极和阴极电极,阳极电极包括多块平行设置的阳极板,阴极电极包括多块平行设置的阴极板,阳极板插入阴极板内相互错开设置,阳极板和阴极板之间以1:1的体积比填充活性炭与绝缘粒子作为复极性第三极,阳极板和阴极板之间的开口部分均通过绝缘隔网封闭,电解池内设置超声棒。复极性第三极可以吸附有机物,通过吸附、降解循环的方式不受吸附饱和量的影响;提高了电解槽单位体积下的有效反应表面积,传质效果增强,有助于废水处理效率的提高;降低了短路电流的产生,提高了电流效率。且设置超声棒,通过超声作用提高电解产生的活性基团的利用率,提高废水的处理效率。

Figure 202010873397

The invention provides a high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes, comprising an electrolytic cell, an anode electrode and a cathode electrode. The anode electrode includes a plurality of anode plates arranged in parallel, and the cathode electrode includes a plurality of cathode plates arranged in parallel. The cathode plates are staggered from each other, and the anode plate and the cathode plate are filled with activated carbon and insulating particles in a volume ratio of 1:1 as the third pole of complex polarity. The openings between the anode plate and the cathode plate are closed by an insulating screen , an ultrasonic rod is set in the electrolytic cell. The pleiotropic third pole can adsorb organic matter, and is not affected by the adsorption saturation through the adsorption and degradation cycle; the effective reaction surface area per unit volume of the electrolytic cell is improved, the mass transfer effect is enhanced, and the efficiency of wastewater treatment is improved. ; Reduce the generation of short-circuit current and improve the current efficiency. In addition, an ultrasonic rod is arranged to improve the utilization rate of active groups generated by electrolysis through ultrasonic action, and improve the treatment efficiency of wastewater.

Figure 202010873397

Description

带三维电极的高氯高氨氮废水处理装置High chlorine and high ammonia nitrogen wastewater treatment device with three-dimensional electrode

技术领域technical field

本发明涉及废水处理领域,特别涉及带三维电极的高氯高氨氮废水处理装置。The invention relates to the field of wastewater treatment, in particular to a high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes.

背景技术Background technique

氨氮是造成水体富营养化的重要因素之一,随着废水排放标准的日益提高,去除废水中残留氨氮的要求和需求越来越高。从工业废水中去除氨氮已有多种方法,折点加氯法由于简单易行而经常被采用。现有技术中,由于液体中含有较多的氨氮成分,使得加大人工处理难度,如气味难闻,并且气味浓度较大的现象。Ammonia nitrogen is one of the important factors causing water eutrophication. With the increasing standards of wastewater discharge, the requirements and demands for removing residual ammonia nitrogen in wastewater are getting higher and higher. There are many methods for removing ammonia nitrogen from industrial wastewater, and the breakpoint chlorination method is often used because of its simplicity. In the prior art, since the liquid contains a lot of ammonia nitrogen components, the difficulty of manual treatment is increased, such as the phenomenon of unpleasant smell and high odor concentration.

电催化氧化技术通过产生羟基自由基等强氧化性的活性基团来降解废水中的有机污染物,具有无二次污染、成本低、适用性强、效率高等特点,在处理高浓度、难生化降解废水方面具有应用潜力。Electrocatalytic oxidation technology degrades organic pollutants in wastewater by generating strong oxidative active groups such as hydroxyl radicals. It has the characteristics of no secondary pollution, low cost, strong applicability and high efficiency. It has application potential in the degradation of wastewater.

但直接采用电解方式能耗高,且针对氨氮废水效率较低。However, the direct electrolysis method has high energy consumption and low efficiency for ammonia nitrogen wastewater.

发明内容SUMMARY OF THE INVENTION

针对现有技术存在的不足,本发明的目的在于提供一种带三维电极的高氯高氨氮废水处理装置,耗能少,处理效率高。In view of the deficiencies in the prior art, the purpose of the present invention is to provide a high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes, which consumes less energy and has high treatment efficiency.

本发明的上述技术目的是通过以下技术方案得以实现的:一种带三维电极的高氯高氨氮废水处理装置,包括电解池、位于电解池内的阳极电极和阴极电极,所述阳极电极为析氯型DSA电极,所述阴极电极为钛板或不锈钢板或石墨板,所述阳极电极由多块平行设置的阳极板通过连接阳板连接而成,所述阴极电极由多块平行设置的阴极板通过连接阴板连接而成,所述阳极板插入阴极板内相互错开设置,所述阳极板和阴极板之间以1:1的体积比填充活性炭与绝缘粒子作为复极性第三极,阳极板和阴极板之间的开口部分均通过绝缘隔网封闭,电解池内设置超声棒,位于阳极电极和阴极电极旁边。The above-mentioned technical purpose of the present invention is achieved through the following technical solutions: a high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes, comprising an electrolytic cell, an anode electrode and a cathode electrode located in the electrolytic cell, and the anode electrode is a chlorine-evolution Type DSA electrode, the cathode electrode is a titanium plate or a stainless steel plate or a graphite plate, the anode electrode is formed by connecting a plurality of parallel anode plates through connecting anode plates, and the cathode electrode is formed by a plurality of parallel cathode plates. It is formed by connecting negative plates. The anode plates are inserted into the cathode plates and arranged to be staggered from each other. The anode plate and the cathode plate are filled with activated carbon and insulating particles in a volume ratio of 1:1 as the third pole of complex polarity. The openings between the plate and the cathode plate are all closed by an insulating screen, and an ultrasonic rod is arranged in the electrolytic cell, which is located beside the anode electrode and the cathode electrode.

复极性第三极作用有如下三点:第一,有一定的吸附作用,活性炭的强吸附性可使有机物在其表面吸附,然后在电场作用下吸附在表面的有机物被氧化降解,之后有机物又继续吸附在活性炭表面,如此吸附-降解-吸附,不受吸附饱和量的影响;第二,提高了电解槽单位体积下的有效反应表面积,传质效果增强,有助于废水处理效率的提高;第三,降低了短路电流的产生,提高了电流效率。且设置超声棒,通过超声作用提高电解产生的活性基团的利用率,提高废水的处理效率。The effect of the pleiotropic third pole has the following three points: First, it has a certain adsorption effect. The strong adsorption of activated carbon can make the organic matter adsorb on its surface, and then the organic matter adsorbed on the surface is oxidized and degraded under the action of the electric field, and then the organic matter is adsorbed on the surface. It continues to be adsorbed on the surface of activated carbon, so adsorption-degradation-adsorption is not affected by the adsorption saturation; secondly, the effective reaction surface area per unit volume of the electrolytic cell is improved, and the mass transfer effect is enhanced, which is conducive to the improvement of wastewater treatment efficiency. ; Third, the generation of short-circuit current is reduced, and the current efficiency is improved. In addition, an ultrasonic rod is arranged to improve the utilization rate of active groups generated by electrolysis through ultrasonic action, and improve the treatment efficiency of wastewater.

阳极板和阴极板之间的开口部分均通过绝缘隔网封闭,使得活性炭和绝缘粒子均被限制在阳极板、阴极板以及绝缘隔网形成的填充空间内,使得废水在流动的时候对填料不会存在影响,同时废水能够通过绝缘隔网的网孔进入填料内。The openings between the anode plate and the cathode plate are closed by the insulating separator, so that the activated carbon and insulating particles are confined in the filling space formed by the anode plate, the cathode plate and the insulating separator, so that the waste water does not affect the filler when it flows. There will be an impact, and the waste water can enter the packing through the mesh of the insulating screen.

进一步的,所述电解池还设置一浮渣清理装置和浮渣聚集装置,所述浮渣聚集装置包括依次连接的进水管、水泵和出水管,所述进水管远离水泵的一端插入电解池的废水内,且进水管插入废水内的一端固定滤网,所述出水管设置在电解池远离进水管的一端;所述浮渣收集装置包括浮渣收集滤斗、固定在电解池上的安装板、固定在安装板上的安装柱、固定在安装柱上的卷扬机,所述卷扬机的拉绳与浮渣收集滤斗固定,所述浮渣收集滤斗与电解池侧壁抵接,浮渣收集滤斗位于进水管一端,所述浮渣收集滤斗开设供进水管穿过的通孔。Further, the electrolytic cell is also provided with a scum cleaning device and a scum accumulation device, the scum accumulation device includes a water inlet pipe, a water pump and a water outlet pipe connected in sequence, and the end of the water inlet pipe away from the water pump is inserted into the electrolytic cell. waste water, and one end of the water inlet pipe inserted into the waste water is fixed with a filter screen, and the water outlet pipe is arranged at one end of the electrolytic cell away from the water inlet pipe; the scum collection device includes a scum collection filter bucket, a mounting plate fixed on the electrolytic cell, The installation column fixed on the installation plate and the hoist fixed on the installation column, the pulling rope of the hoist is fixed with the scum collection filter hopper, the scum collection filter hopper is in contact with the side wall of the electrolytic cell, and the scum collection filter The bucket is located at one end of the water inlet pipe, and the scum collection filter bucket is provided with a through hole for the water inlet pipe to pass through.

水泵启动,水从进水管进入,出水管回流至电解池,浮渣受水流的影响汇聚在进水管一侧,之后通过卷扬机将浮渣收集滤斗吊起去除浮渣。When the water pump starts, water enters from the water inlet pipe, and the water outlet pipe returns to the electrolytic cell. The scum is collected on one side of the water inlet pipe under the influence of the water flow, and then the scum collection filter bucket is lifted by the winch to remove the scum.

进一步的,所述安装板上固定一电机,所述电机的输出轴上固定一连接杆,所述连接杆上固定一顶块。Further, a motor is fixed on the mounting plate, a connecting rod is fixed on the output shaft of the motor, and a top block is fixed on the connecting rod.

当浮渣收集滤斗至电解池顶部时,电机启动带动连接杆,连接杆转动带动顶块,顶块带动浮渣收集滤斗旋转,使得浮渣倾倒出来。When the scum collection filter hopper reaches the top of the electrolytic cell, the motor starts to drive the connecting rod, the connecting rod rotates to drive the top block, and the top block drives the scum collection filter hopper to rotate, so that the scum is poured out.

进一步的,所述电解池底部安装曝气装置,所述曝气装置包括曝气管、与曝气管连接的空压机。所述曝气管在电解池内设置多个。Further, an aeration device is installed at the bottom of the electrolytic cell, and the aeration device includes an aeration pipe and an air compressor connected to the aeration pipe. A plurality of the aeration pipes are arranged in the electrolytic cell.

曝气利于均匀水质,防止电极结垢。Aeration is conducive to uniform water quality and prevents electrode scaling.

进一步的,所述电解池位于进水管一侧设置有浮渣收集池,所述进水管穿过浮渣收集池。Further, the electrolytic cell is provided with a scum collection tank on one side of the water inlet pipe, and the water inlet pipe passes through the scum collection tank.

综上所述,本发明具有以下有益效果:本发明有效提升废水处理效率、节能、同时方便快速清理浮渣。To sum up, the present invention has the following beneficial effects: the present invention effectively improves wastewater treatment efficiency, saves energy, and at the same time facilitates and quickly cleans scum.

附图说明Description of drawings

图1是实施例的结构示意图;Fig. 1 is the structural representation of embodiment;

图2是电解池的结构示意图;Fig. 2 is the structural representation of electrolytic cell;

图3是去除浮渣时的状态图。FIG. 3 is a state diagram when scum is removed.

附图标记:1、电解池;2、阳极电极;21、阳极板;22、连接阳板;3、阴极电极;31、阴极板;32、连接阴板;4、超声棒;51、进水管;52、水泵;53、出水管;6、浮渣收集滤斗;71、安装板;72、安装柱;73、卷扬机;81、电机;82、连接杆;83、顶块;91、曝气管;92、空压机;93、浮渣收集池;10、绝缘隔网。Reference numerals: 1. Electrolysis cell; 2. Anode electrode; 21. Anode plate; 22. Connecting anode plate; 3. Cathode electrode; 31. Cathode plate; 32. Connecting cathode plate; 4. Ultrasonic rod; 51. Water inlet pipe ;52, water pump; 53, water outlet pipe; 6, scum collection filter bucket; 71, mounting plate; 72, mounting column; 73, winch; 81, motor; 82, connecting rod; 83, top block; 91, aeration pipe; 92, air compressor; 93, scum collection tank; 10, insulating screen.

具体实施方式Detailed ways

本具体实施例仅仅是对本发明的解释,其并不是对本发明的限制,本领域技术人员在阅读完本说明书后可以根据需要对本实施例做出没有创造性贡献的修改,但只要在本发明的权利要求范围内都受到专利法的保护。This specific embodiment is only an explanation of the present invention, and it does not limit the present invention. Those skilled in the art can make modifications without creative contribution to the present embodiment as required after reading this specification, but as long as the rights of the present invention are used All claims are protected by patent law.

一种带三维电极的高氯高氨氮废水处理装置,包括电解池1、位于电解池1内的阳极电极2和阴极电极3,所述阳极电极2为析氯型DSA电极,所述阴极电极3为钛板或不锈钢板或石墨板。所述阳极电极2由多块平行设置的阳极板21通过连接阳板22连接而成,阳极板21和连接阳板22均为铁板。阴极电极3由多块平行设置的阴极板31通过连接阴板32连接而成,阴极板31和连接阴板32均为碳板。阳极板21插入阴极板31内相互错开设置,所述阳极板21和阴极板31之间以1:1的体积比填充活性炭与绝缘粒子作为复极性第三极,绝缘粒子为TO绝缘粒子,阳极板21和阴极板31之间的开口部分均通过绝缘隔网10封闭。所述电解池1内设置超声棒4,超声棒4位于阳极电极2和阴极电极3旁边。A high-chlorine and high-ammonia-nitrogen wastewater treatment device with a three-dimensional electrode, comprising an electrolytic cell 1, an anode electrode 2 and a cathode electrode 3 located in the electrolytic cell 1, the anode electrode 2 is a chlorine-evolution DSA electrode, and the cathode electrode 3 For titanium plate or stainless steel plate or graphite plate. The anode electrode 2 is formed by connecting a plurality of parallel anode plates 21 through connecting anode plates 22, and both anode plates 21 and connecting anode plates 22 are iron plates. The cathode electrode 3 is formed by connecting a plurality of parallel cathode plates 31 through connecting cathode plates 32 , and both the cathode plates 31 and the connecting cathode plates 32 are carbon plates. The anode plate 21 is inserted into the cathode plate 31 and arranged staggered from each other. The anode plate 21 and the cathode plate 31 are filled with activated carbon and insulating particles in a volume ratio of 1:1 as the third pole of the complex polarity, and the insulating particles are TO insulating particles. The opening portions between the anode plate 21 and the cathode plate 31 are all closed by the insulating screen 10 . An ultrasonic rod 4 is arranged in the electrolytic cell 1 , and the ultrasonic rod 4 is located beside the anode electrode 2 and the cathode electrode 3 .

电解池1还设置一浮渣清理装置和浮渣聚集装置,所述浮渣聚集装置包括依次连接的进水管51、水泵52和出水管53,所述进水管51远离水泵52的一端紧贴电解池1内壁插入电解池1的废水内,且进水管51插入废水内的一端固定滤网,滤网保证水泵52抽水顺畅。出水管53设置在电解池1远离进水管51的一端。出水管53的出水口高度高于进水管51的进水口高度。The electrolytic cell 1 is also provided with a scum cleaning device and a scum accumulation device. The scum accumulation device includes a water inlet pipe 51, a water pump 52 and a water outlet pipe 53 connected in sequence, and the end of the water inlet pipe 51 away from the water pump 52 is close to the electrolysis device. The inner wall of the pool 1 is inserted into the waste water of the electrolysis cell 1, and one end of the water inlet pipe 51 inserted into the waste water is fixed with a filter screen, which ensures that the water pump 52 can pump water smoothly. The water outlet pipe 53 is arranged at one end of the electrolytic cell 1 away from the water inlet pipe 51 . The height of the water outlet of the water outlet pipe 53 is higher than that of the water inlet of the water inlet pipe 51 .

浮渣收集装置包括浮渣收集滤斗6、固定在电解池1上的安装板71、固定在安装板71上的安装柱72、固定在安装柱72上的卷扬机73,所述卷扬机73的拉绳与浮渣收集滤斗6固定,浮渣收集滤斗6位于进水管51一端,所述浮渣收集滤斗6与电解池1侧壁抵接,浮渣收集滤斗6相对与进水管51紧贴一面的池壁开口设置,其余三面均形成侧壁,如此方便浮渣倾倒。所述浮渣收集滤斗6开设供进水管51穿过的通孔。安装板71上固定一电机81,所述电机81的输出轴上固定一连接杆82,所述连接杆82上固定一顶块83。The scum collection device includes a scum collection filter hopper 6, a mounting plate 71 fixed on the electrolytic cell 1, a mounting column 72 fixed on the mounting plate 71, and a hoist 73 fixed on the mounting column 72. The rope is fixed with the scum collection filter hopper 6, the scum collection filter hopper 6 is located at one end of the water inlet pipe 51, the scum collection filter hopper 6 is in contact with the side wall of the electrolytic cell 1, and the scum collection filter hopper 6 is opposite to the water inlet pipe 51. The opening of the pool wall close to one side is arranged, and the other three sides are formed with side walls, which is convenient for the scum dumping. The scum collection filter hopper 6 has a through hole for the water inlet pipe 51 to pass through. A motor 81 is fixed on the mounting plate 71 , a connecting rod 82 is fixed on the output shaft of the motor 81 , and a top block 83 is fixed on the connecting rod 82 .

所述电解池1底部安装曝气装置,所述曝气装置包括曝气管91、与曝气管91连接的空压机92。曝气管91穿过电解池1伸入废水中,曝气管91在电解池1内设置多个。电解池1位于进水管51一侧设置有浮渣收集池93,进水管51穿过浮渣收集池93。An aeration device is installed at the bottom of the electrolytic cell 1 , and the aeration device includes an aeration pipe 91 and an air compressor 92 connected to the aeration pipe 91 . The aeration pipes 91 extend through the electrolytic cell 1 into the waste water, and a plurality of aeration pipes 91 are arranged in the electrolytic cell 1 . The electrolytic cell 1 is provided with a scum collection tank 93 on one side of the water inlet pipe 51 , and the water inlet pipe 51 passes through the scum collection tank 93 .

水泵52启动,水从进水管51进入,出水管53回流至电解池1,浮渣受水流的影响汇聚在进水管51一侧,之后通过卷扬机73将浮渣收集滤斗6吊起。当浮渣收集滤斗6至电解池1顶部时,电机81启动带动连接杆82,连接杆82转动带动顶块83,顶块83带动浮渣收集滤斗6旋转,使得浮渣倾倒出来进入浮渣收集池93。The water pump 52 is started, the water enters from the water inlet pipe 51, the water outlet pipe 53 returns to the electrolytic cell 1, and the scum is collected on one side of the water inlet pipe 51 under the influence of the water flow, and then the scum collection filter hopper 6 is hoisted by the hoist 73. When the scum collection filter hopper 6 reaches the top of the electrolytic cell 1, the motor 81 starts to drive the connecting rod 82, the connecting rod 82 rotates and drives the top block 83, and the top block 83 drives the scum collection filter hopper 6 to rotate, so that the scum is poured out into the float Slag collection tank 93.

Claims (7)

1.一种带三维电极的高氯高氨氮废水处理装置,包括电解池(1)、位于电解池(1)内的阳极电极(2)和阴极电极(3),所述阳极电极(2)为析氯型DSA电极,所述阴极电极(3)为钛板或不锈钢板或石墨板,其特征在于:所述阳极电极(2)由多块平行设置的阳极板(21)通过连接阳板(22)连接而成,所述阴极电极(3)由多块平行设置的阴极板(31)通过连接阴板(32)连接而成,所述阳极板(21)插入阴极板(31)内相互错开设置,所述阳极板(21)和阴极板(31)之间以1:1的体积比填充活性炭与绝缘粒子作为复极性第三极,所述阳极板(21)和阴极板(31)之间的开口部分均通过绝缘隔网(10)封闭,所述电解池(1)内设置超声棒(4),超声棒(4)位于阳极电极(2)和阴极电极(3)旁边。1. A high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrode, comprising an electrolytic cell (1), an anode electrode (2) and a cathode electrode (3) positioned in the electrolytic cell (1), the anode electrode (2) It is a chlorine-dissolving type DSA electrode, and the cathode electrode (3) is a titanium plate or a stainless steel plate or a graphite plate, and it is characterized in that: the anode electrode (2) is connected by a plurality of parallel anode plates (21) by connecting the anode plates. (22) connected, the cathode electrode (3) is formed by connecting a plurality of parallel cathode plates (31) by connecting the cathode plates (32), and the anode plate (21) is inserted into the cathode plate (31) They are arranged staggered from each other, and the anode plate (21) and the cathode plate (31) are filled with activated carbon and insulating particles in a volume ratio of 1:1 as the third pole of complex polarity, the anode plate (21) and the cathode plate (31). 31) The openings between are all closed by the insulating screen (10), an ultrasonic rod (4) is arranged in the electrolytic cell (1), and the ultrasonic rod (4) is located beside the anode electrode (2) and the cathode electrode (3) . 2.根据权利要求1的带三维电极的高氯高氨氮废水处理装置,其特征在于:所述电解池(1)还设置一浮渣清理装置和浮渣聚集装置,所述浮渣聚集装置包括依次连接的进水管(51)、水泵(52)和出水管(53),所述进水管(51)远离水泵(52)的一端插入电解池(1)的废水内,且进水管(51)插入废水内的一端固定滤网,所述出水管(53)设置在电解池(1)远离进水管(51)的一端;所述浮渣收集装置包括浮渣收集滤斗(6)、固定在电解池(1)上的安装板(71)、固定在安装板(71)上的安装柱(72)、固定在安装柱(72)上的卷扬机(73),所述卷扬机(73)的拉绳与浮渣收集滤斗(6)固定,所述浮渣收集滤斗(6)与电解池(1)侧壁抵接,浮渣收集滤斗(6)位于进水管(51)一端,所述浮渣收集滤斗(6)开设供进水管(51)穿过的通孔。2. The high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrode according to claim 1, characterized in that: the electrolytic cell (1) is also provided with a scum cleaning device and a scum gathering device, and the scum gathering device comprises: The water inlet pipe (51), the water pump (52) and the water outlet pipe (53) are connected in sequence, and one end of the water inlet pipe (51) away from the water pump (52) is inserted into the waste water of the electrolytic cell (1), and the water inlet pipe (51) A filter screen is fixed at one end inserted into the waste water, and the water outlet pipe (53) is arranged at one end of the electrolytic cell (1) away from the water inlet pipe (51); The mounting plate (71) on the electrolytic cell (1), the mounting column (72) fixed on the mounting plate (71), and the hoist (73) fixed on the mounting column (72), the The rope is fixed with the scum collection filter hopper (6), the scum collection filter hopper (6) is in contact with the side wall of the electrolytic cell (1), and the scum collection filter hopper (6) is located at one end of the water inlet pipe (51). The scum collection filter hopper (6) is provided with a through hole for the water inlet pipe (51) to pass through. 3.根据权利要求2的带三维电极的高氯高氨氮废水处理装置,其特征在于:所述安装板(71)上固定一电机(81),所述电机(81)的输出轴上固定一连接杆(82),所述连接杆(82)上固定一顶块(83)。3. The high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes according to claim 2, wherein a motor (81) is fixed on the mounting plate (71), and a motor (81) is fixed on the output shaft of the motor (81). A connecting rod (82), a top block (83) is fixed on the connecting rod (82). 4.根据权利要求1的带三维电极的高氯高氨氮废水处理装置,其特征在于:所述电解池(1)底部安装曝气装置,所述曝气装置包括曝气管(91)、与曝气管(91)连接的空压机(92)。4. The high-chlorine and high-ammonia nitrogen wastewater treatment device with three-dimensional electrode according to claim 1, characterized in that: an aeration device is installed at the bottom of the electrolytic cell (1), and the aeration device comprises an aeration pipe (91), and The air compressor (92) to which the aeration pipe (91) is connected. 5.根据权利要求4的带三维电极的高氯高氨氮废水处理装置,其特征在于:所述曝气管(91)在电解池(1)内设置多个。5. The high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes according to claim 4, characterized in that: a plurality of said aeration pipes (91) are arranged in the electrolytic cell (1). 6.根据权利要求3的带三维电极的高氯高氨氮废水处理装置,其特征在于:所述电解池(1)位于进水管(51)一侧设置有浮渣收集池(93)。6. The high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes according to claim 3, wherein the electrolytic cell (1) is provided with a scum collection tank (93) on one side of the water inlet pipe (51). 7.根据权利要求6的带三维电极的高氯高氨氮废水处理装置,其特征在于:所述进水管(51)穿过浮渣收集池(93)。7. The high-chlorine and high-ammonia-nitrogen wastewater treatment device with three-dimensional electrodes according to claim 6, wherein the water inlet pipe (51) passes through the scum collection tank (93).
CN202010873397.0A 2020-08-26 2020-08-26 High-chlorine high-ammonia nitrogen wastewater treatment device with three-dimensional electrode Pending CN111943329A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20090002944A (en) * 2007-07-05 2009-01-09 한국수자원공사 Pressure flotation filter paper
CN108295534A (en) * 2018-04-10 2018-07-20 重庆亚领环保科技有限公司 Treatment tank scum collection system
CN209367877U (en) * 2018-12-11 2019-09-10 武汉创美优达环保科技发展有限公司 A multi-dimensional electrocatalytic oxidation device
CN210993325U (en) * 2019-11-01 2020-07-14 江苏源盛环保设备有限公司 Residue processing apparatus for industrial sewage treatment
CN212334691U (en) * 2020-08-26 2021-01-12 广东石油化工学院 High chlorine and high ammonia nitrogen wastewater treatment device with three-dimensional electrode

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20090002944A (en) * 2007-07-05 2009-01-09 한국수자원공사 Pressure flotation filter paper
CN108295534A (en) * 2018-04-10 2018-07-20 重庆亚领环保科技有限公司 Treatment tank scum collection system
CN209367877U (en) * 2018-12-11 2019-09-10 武汉创美优达环保科技发展有限公司 A multi-dimensional electrocatalytic oxidation device
CN210993325U (en) * 2019-11-01 2020-07-14 江苏源盛环保设备有限公司 Residue processing apparatus for industrial sewage treatment
CN212334691U (en) * 2020-08-26 2021-01-12 广东石油化工学院 High chlorine and high ammonia nitrogen wastewater treatment device with three-dimensional electrode

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