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 PDFInfo
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 17
- 239000000460 chlorine Substances 0.000 title claims abstract description 13
- 229910052801 chlorine Inorganic materials 0.000 title claims abstract description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000002351 wastewater Substances 0.000 claims abstract description 16
- 239000002245 particle Substances 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 60
- 238000005273 aeration Methods 0.000 claims description 18
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 229910002804 graphite Inorganic materials 0.000 claims description 3
- 239000010439 graphite Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000010936 titanium Substances 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- 238000005868 electrolysis reaction Methods 0.000 abstract description 6
- 238000001179 sorption measurement Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 4
- 239000005416 organic matter Substances 0.000 abstract description 4
- 230000015556 catabolic process Effects 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 238000006731 degradation reaction Methods 0.000 abstract description 2
- 230000004983 pleiotropic effect Effects 0.000 abstract description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 5
- 238000009825 accumulation Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/4602—Treatment of water, waste water, or sewage by electrochemical methods for prevention or elimination of deposits
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/4619—Supplying 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。
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.
Description
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
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
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
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
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
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