CN204675927U - A kind of device of electrochemical oxidation method treatment of dyeing and printing - Google Patents
A kind of device of electrochemical oxidation method treatment of dyeing and printing Download PDFInfo
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- CN204675927U CN204675927U CN201520218973.2U CN201520218973U CN204675927U CN 204675927 U CN204675927 U CN 204675927U CN 201520218973 U CN201520218973 U CN 201520218973U CN 204675927 U CN204675927 U CN 204675927U
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Abstract
本实用新型公开了一种用电化学氧化方法处理印染废水的装置,属于环保技术和废水处理领域。本实用新型装置以掺硼金刚石电极为阳极,不锈钢为阴极,通过将电极设置在电化学反应器内,并让废水在设定的时间内在储水槽与电化学反应器之间不断循环的方法,去除有机物,盐,色度等污染物,使废水达到国家排放标准。该装置具有体积小,效率高,能耗低,可控性好等优点。
The utility model discloses a device for treating printing and dyeing wastewater by an electrochemical oxidation method, which belongs to the field of environmental protection technology and wastewater treatment. The device of the utility model uses a boron-doped diamond electrode as an anode, and stainless steel as a cathode. By setting the electrodes in the electrochemical reactor and allowing the waste water to circulate continuously between the water storage tank and the electrochemical reactor within a set time, Remove organic matter, salt, chroma and other pollutants to make the wastewater meet the national discharge standards. The device has the advantages of small size, high efficiency, low energy consumption and good controllability.
Description
技术领域technical field
本实用新型所涉及的处理污水的装置及其方法,属于环保技术领域和废水处理技术领域。The sewage treatment device and method thereof involved in the utility model belong to the technical field of environmental protection and the technical field of waste water treatment.
背景技术Background technique
印染废水是环保行业公认的最难处理的废水之一。它色度高,有机物浓度大,成分复杂,难降解有机物多,而且由于着色工艺的需要,常含有大量的无机盐类,可生化性差。目前印染废水的处理方法有物理、化学、生物方法或多种方法联合,生物处理法对COD的降解率为50%,化学沉淀法和气浮法对COD的降解率仅30%。因此,开发经济、有效的印染废水处理工艺日益成为当前环保行业关注和研究的课题。Printing and dyeing wastewater is recognized by the environmental protection industry as one of the most difficult wastewater to treat. It has high chroma, high concentration of organic matter, complex components, and many refractory organic matter. Due to the needs of the coloring process, it often contains a large amount of inorganic salts and has poor biodegradability. At present, the treatment methods of printing and dyeing wastewater include physical, chemical, biological methods or a combination of multiple methods. The degradation rate of COD by biological treatment is 50%, and the degradation rate of COD by chemical precipitation and air flotation is only 30%. Therefore, the development of economical and effective printing and dyeing wastewater treatment processes has increasingly become a topic of concern and research in the current environmental protection industry.
与传统工艺相比,电化学氧化技术适宜处理含高浓度有机物,高盐的废水。通过在电极表面产生的羟基自由基无选择地直接与废水中的有机污染物反应,将其降解为二氧化碳、水和简单有机物,不需另外添加氧化还原剂,没有或很少产生二次污染,是一种氧化能力较强、降解效率高、便于自动化、反应条件温和、设备及其操作较为简单的技术,在印染废水处理方面极具潜力。Compared with the traditional process, electrochemical oxidation technology is suitable for treating wastewater with high concentration of organic matter and high salt. The hydroxyl radicals generated on the surface of the electrode directly react with the organic pollutants in the wastewater without selection, and degrade them into carbon dioxide, water and simple organic matter, without adding additional redox agents, and there is no or little secondary pollution. It is a technology with strong oxidation ability, high degradation efficiency, easy automation, mild reaction conditions, relatively simple equipment and operation, and has great potential in the treatment of printing and dyeing wastewater.
电极材料对于电化学氧化技术非常重要,它的性能直接决定了电化学氧化过程的效果和效率。目前使用的电极材料有很多不足之处,如石墨电极,对有机物降解能力差,电流效率低,易膨胀、脱落,贵金属电极如Pt、Au等成本高,易被硫化物毒化而失去电催化能力。掺硼金刚石电极是目前研究表明电化学性能最好且最为稳定的电极材料。Electrode material is very important for electrochemical oxidation technology, its performance directly determines the effect and efficiency of electrochemical oxidation process. The electrode materials currently used have many shortcomings, such as graphite electrodes, which have poor degradation ability to organic matter, low current efficiency, easy expansion and falling off, and noble metal electrodes such as Pt and Au have high cost and are easily poisoned by sulfide and lose their electrocatalytic ability. . Boron-doped diamond electrode is the electrode material with the best electrochemical performance and the most stable.
传统的电化学反应器由于设计不合理,电流效率低,成本高。合理的反应器设计可以有效的强化羟基自由基与污染物的接触,提高电流效率,降低运行时间和成本。Traditional electrochemical reactors have low current efficiency and high cost due to unreasonable design. Reasonable reactor design can effectively strengthen the contact between hydroxyl radicals and pollutants, improve current efficiency, and reduce operating time and cost.
实用新型内容Utility model content
本实用新型的目的在于克服现有技术中存在的不足之处,提供一种高效的,设计合理的处理印染废水的装置。The purpose of the utility model is to overcome the deficiencies in the prior art and provide an efficient and reasonably designed device for treating printing and dyeing wastewater.
一种用电化学氧化方法处理印染废水的装置包括储水槽、水泵、恒流稳压电源、电化学反应器、袋式过滤器、自动控制器;储水槽、水泵、电化学反应器、袋式过滤器依次连接;电化学反应器包括外壳和电极组件两部分,其中电极组件为核心装置,以掺硼金刚石电极为阳极,不锈钢电极为阴极;阳极和阴极互相平行,垂直放置于反应器内。A device for treating printing and dyeing wastewater by electrochemical oxidation includes a water storage tank, a water pump, a constant current and voltage stabilized power supply, an electrochemical reactor, a bag filter, and an automatic controller; a water storage tank, a water pump, an electrochemical reactor, a bag type The filter is connected in sequence; the electrochemical reactor consists of two parts: the shell and the electrode assembly. The electrode assembly is the core device, with the boron-doped diamond electrode as the anode and the stainless steel electrode as the cathode; the anode and cathode are parallel to each other and placed vertically in the reactor.
废水在设定的时间内不断循环通过电化学反应器,袋式过滤器及储水槽。The waste water is continuously circulated through the electrochemical reactor, bag filter and storage tank for a set time.
废水经电化学氧化后的出水流经一个袋式过滤器,除去沉淀和悬浮物。The effluent after electrochemical oxidation of wastewater flows through a bag filter to remove sediment and suspended matter.
其内部设置的掺硼金刚石电极板尺寸为250mm x 500mm。The size of the boron-doped diamond electrode plate set inside it is 250mm x 500mm.
电化学反应器中电极板在通电后,可产生大量羟基自由基(·OH),自由基具有强氧化性,可将废水中有机物完全降解;降解过程中产生的沉淀物及气体由袋式过滤器滤除。经过设定的1小时的实验时间后,结果列于表1中:After the electrode plate in the electrochemical reactor is energized, a large number of hydroxyl radicals (OH) can be generated. The free radicals have strong oxidizing properties and can completely degrade the organic matter in the wastewater; the sediment and gas generated during the degradation process are filtered by the bag filter out. After the set experiment time of 1 hour, the results are listed in Table 1:
表1.某工厂印染废水经本实用新型装置处理后的结果及耗能情况Table 1. Results and energy consumption of printing and dyeing wastewater from a certain factory after being treated by the utility model device
本实用新型与现有技术相比,具有如下一些独特的优点:①该装置设计合理,电极板面积大,处理效率高,体积小,耗时少;②自控性高,通过电压电流的调节可以很好的控制电化学氧化过程;③掺硼金刚石电极析氧电势高,抑制了析氧副反应的发生,有利于羟基自由基(·OH)等具有强氧化能力的活性中间体生成,从而具有较高的电流效率,能耗少;④掺硼金刚石电极,化学性能稳定,吸附性小,具有“自洁净”能力,使用寿命长,成本低。Compared with the prior art, the utility model has some unique advantages as follows: ① The device has reasonable design, large electrode plate area, high processing efficiency, small volume, and less time-consuming; The electrochemical oxidation process is well controlled; ③The boron-doped diamond electrode has a high oxygen evolution potential, which inhibits the occurrence of oxygen evolution side reactions, and is conducive to the generation of active intermediates with strong oxidizing ability such as hydroxyl radicals (OH), thus having Higher current efficiency, less energy consumption; ④ boron-doped diamond electrode, stable chemical performance, low adsorption, "self-cleaning" ability, long service life and low cost.
附图说明Description of drawings
图1为本实用新型的装置示意图。Fig. 1 is the device schematic diagram of the present utility model.
图中,1、储水槽,2、水泵,3、恒流稳压电源,4、自动控制器,5、电化学反应器,6、袋式过滤器。In the figure, 1. Water storage tank, 2. Water pump, 3. Constant current and voltage stabilized power supply, 4. Automatic controller, 5. Electrochemical reactor, 6. Bag filter.
具体实施方式Detailed ways
下面结合具体实施例对本实用新型所述装置及其方法进一步说明。The device and method of the present invention will be further described below in conjunction with specific embodiments.
废水首先进入(1)储水槽,经过(2)水泵送入(5)电化学反应器;(3)恒流稳压电源向(5)电化学反应器供电后,电化学反应器中会产生强氧化性物质氧化水中污染物,之后流入(6)袋式过滤器;由于废水中污染物浓度高,需要在(5)电化学反应器、(1)储水槽、(6)袋式过滤器之间不断循环,经在线监测水质达标后,由(4)自动控制器控制,停止循环过程,由(1)储水槽排出。The waste water first enters (1) the water storage tank, and is sent to (5) the electrochemical reactor through the (2) water pump; Strong oxidizing substances oxidize pollutants in the water, and then flow into (6) bag filter; due to the high concentration of pollutants in wastewater, it needs to be in (5) electrochemical reactor, (1) water storage tank, (6) bag filter Continuously circulate between them, after the online monitoring water quality reaches the standard, it will be controlled by (4) automatic controller, stop the circulation process, and discharge from (1) water storage tank.
以6块250x 500mm的BDD掺硼金刚石电极为阳级,相同大小的6块不锈钢电极为阴极,电流密度20mA·cm-2.储水池中的某印染厂废水1000L经水泵以50L/min的流速,流入到电化学反应器中,恒流稳压电源向电化学反应器提供一定的电流电压,在BDD电极表面产生羟基自由基(·OH)等强氧化剂,可有效去除废水中的污染物,处理后的水从反应器上部经过袋式过滤器,除去沉淀和悬浮物质,再流入储水槽中,这样不断的循环。Six 250x 500mm BDD boron-doped diamond electrodes are used as anodes, and six stainless steel electrodes of the same size are used as cathodes. The current density is 20mA·cm -2 . 1000L of wastewater from a printing and dyeing factory in the storage tank is pumped at a flow rate of 50L/min. , flows into the electrochemical reactor, the constant current regulated power supply provides a certain current and voltage to the electrochemical reactor, and generates strong oxidants such as hydroxyl radicals (OH) on the surface of the BDD electrode, which can effectively remove pollutants in wastewater. The treated water passes through the bag filter from the upper part of the reactor to remove sediment and suspended matter, and then flows into the water storage tank, so that it circulates continuously.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106006850A (en) * | 2016-05-25 | 2016-10-12 | 安徽普氏生态环境工程有限公司 | Method for performing electrochemical oxidative degradation on sewage COD (chemical oxygen demand) by using boron-doped graphene electrode |
CN106145460A (en) * | 2015-04-10 | 2016-11-23 | 北京中力信达环保工程有限公司 | A kind of electrochemical oxidation method processes the device of dyeing waste water |
CN106277487A (en) * | 2016-10-26 | 2017-01-04 | 北京中力信达环保工程有限公司 | A kind of electrochemicial oxidation desulfurization wastewater device |
CN108231234A (en) * | 2017-12-29 | 2018-06-29 | 中国工程物理研究院材料研究所 | The electrochemicial oxidation device and electrochemical oxidation method for treating of a kind of Spent Radioactive machine oil |
CN110342694A (en) * | 2018-04-03 | 2019-10-18 | 华东理工大学 | A kind of processing method of electroplating wastewater |
CN113860595A (en) * | 2021-11-12 | 2021-12-31 | 江苏雄安环保科技有限公司 | Multifunctional polar plate coupling electro-catalysis system and paint wastewater treatment method thereof |
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2015
- 2015-04-10 CN CN201520218973.2U patent/CN204675927U/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106145460A (en) * | 2015-04-10 | 2016-11-23 | 北京中力信达环保工程有限公司 | A kind of electrochemical oxidation method processes the device of dyeing waste water |
CN106006850A (en) * | 2016-05-25 | 2016-10-12 | 安徽普氏生态环境工程有限公司 | Method for performing electrochemical oxidative degradation on sewage COD (chemical oxygen demand) by using boron-doped graphene electrode |
CN106277487A (en) * | 2016-10-26 | 2017-01-04 | 北京中力信达环保工程有限公司 | A kind of electrochemicial oxidation desulfurization wastewater device |
CN108231234A (en) * | 2017-12-29 | 2018-06-29 | 中国工程物理研究院材料研究所 | The electrochemicial oxidation device and electrochemical oxidation method for treating of a kind of Spent Radioactive machine oil |
CN108231234B (en) * | 2017-12-29 | 2019-08-02 | 中国工程物理研究院材料研究所 | A kind of the electrochemicial oxidation device and electrochemical oxidation method for treating of Spent Radioactive machine oil |
CN110342694A (en) * | 2018-04-03 | 2019-10-18 | 华东理工大学 | A kind of processing method of electroplating wastewater |
CN113860595A (en) * | 2021-11-12 | 2021-12-31 | 江苏雄安环保科技有限公司 | Multifunctional polar plate coupling electro-catalysis system and paint wastewater treatment method thereof |
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