CN110040887A - A kind of organic liquid waste processing method and processing device - Google Patents

A kind of organic liquid waste processing method and processing device Download PDF

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Publication number
CN110040887A
CN110040887A CN201910389393.2A CN201910389393A CN110040887A CN 110040887 A CN110040887 A CN 110040887A CN 201910389393 A CN201910389393 A CN 201910389393A CN 110040887 A CN110040887 A CN 110040887A
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waste liquid
organic waste
electrolytic cell
pipe
tank
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戚明辉
肖光莉
姚旭松
龙震
徐强
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KEYUAN ENGINEERING TECHNICAL TEST CENTER OF SICHUAN PROVINCE
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KEYUAN ENGINEERING TECHNICAL TEST CENTER OF SICHUAN PROVINCE
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • 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
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • 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
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • 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
    • C02F1/46176Galvanic cells
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention discloses a kind of organic liquid waste processing method and processing devices, the following steps are included: initial filter, electrolysis, coarse filtration and refined filtration, organic liquid waste handles solidification equipment, including electrolytic cell and the lautertuns being connected to electrolytic cell, electrolyte tank is equipped with above the electrolytic cell, the concentration meter that the side wall of upper part of the electrolytic cell is equipped with wastewater feed pipe and is connected in parallel on wastewater feed pipe, light electrolysis device is equipped in electrolytic cell, the bottom of electrolytic tank is equipped with sewage pipe, the side wall of the electrolytic cell is equipped with the drain pipe being connected to lautertuns, the feed end of drain pipe in electrolytic cell is connected with filter core, multiple filtration film is equipped in the lautertuns.Present invention tool is by carrying out light electrolysis to organic liquid waste or electrolyte is added, and increases the flocculate in organic liquid waste, adsorbs the organic matter in organic liquid waste by flocculate, reduces the production cost of enterprise, reduce purifying step.

Description

一种有机废液处理方法及装置A kind of organic waste liquid treatment method and device

技术领域technical field

本发明涉及有机废液处理领域,特别是涉及一种有机废液处理方法及装置。The invention relates to the field of organic waste liquid treatment, in particular to a method and device for organic waste liquid treatment.

背景技术Background technique

有机废液:在生活污水、食品加工和造纸等工业废水中,含有碳水化合物、蛋白质、油脂、木质素等有机物质。这些物质以悬浮或溶解状态存在于污水中,可通过微生物的生物化学作用而分解。在其分解过程中需要消耗氧气,因而被称为耗氧污染物。这种污染物可造成水中溶解氧减少,影响鱼类和其他水生生物的生长。水中溶解氧耗尽后,有机物进行厌氧分解,产生硫化氢、氨和硫醇等难闻气味,使水质恶化。水体中有机物成分非常复杂,耗氧有机物浓度常用单位体积水中耗氧物质生化分解过程中所消耗的氧量表示。目前处理有机废液的处理方法是在废液中加入各种絮凝剂、过滤、再次加入絮凝剂、再次过滤的方式将有机废液中的有机物滤出,这样的处理方式周期长、投入絮凝剂的量较大,增加了有机废液的处理成本。Organic waste liquid: In domestic sewage, food processing and papermaking and other industrial waste water, it contains organic substances such as carbohydrates, proteins, oils, and lignin. These substances are present in the sewage in a suspended or dissolved state and can be decomposed by the biochemical action of microorganisms. Oxygen is consumed in the process of its decomposition, so it is called oxygen-consuming pollutants. This pollutant can reduce dissolved oxygen in the water, affecting the growth of fish and other aquatic life. After the dissolved oxygen in the water is exhausted, the organic matter undergoes anaerobic decomposition, producing unpleasant odors such as hydrogen sulfide, ammonia and mercaptans, which deteriorate the water quality. The composition of organic matter in water is very complex, and the concentration of oxygen-consuming organic matter is usually expressed by the amount of oxygen consumed in the biochemical decomposition of oxygen-consuming substances per unit volume of water. At present, the treatment method of organic waste liquid is to add various flocculants to the waste liquid, filter, add flocculants again, and filter again to filter out the organic matter in the organic waste liquid. The amount of effluent is relatively large, which increases the treatment cost of organic waste liquid.

发明内容SUMMARY OF THE INVENTION

本发明的目的在于提供一种处理成本低、生产周期短的有机废液处理方法及装置。The purpose of the present invention is to provide an organic waste liquid treatment method and device with low treatment cost and short production cycle.

本发明的目的是通过以下技术方案实现的:The purpose of this invention is to realize through the following technical solutions:

一种有机废液处理方法,包括以下步骤:A method for treating organic waste liquid, comprising the following steps:

(1)初滤:对有机废液进行初滤,用于将有机废液中的悬浮物滤出,用于提高电解的效率;(1) primary filtration: carry out primary filtration to the organic waste liquid, for filtering out the suspended matter in the organic waste liquid, for improving the efficiency of electrolysis;

(2)电解:将有机废液引入电解槽,并在电解槽内的有机废液中通入微电流进行电解至有机废液中的有机物沉淀,或在有机废液中加入电解液,加入电解液时需要将电解槽内的有机废液和电解液搅拌均匀后静置至有机废液中的有机物沉淀,通过两种方法沉淀有机废液中的有机物,可灵活的处理有机废液,提高有机废液的处理效率;(2) Electrolysis: the organic waste liquid is introduced into the electrolytic cell, and a microcurrent is passed into the organic waste liquid in the electrolytic cell for electrolysis to the organic matter precipitation in the organic waste liquid, or an electrolyte is added to the organic waste liquid, and the electrolyte is added. When it is necessary to stir the organic waste liquid and electrolyte in the electrolytic cell evenly, let it stand to precipitate the organic matter in the organic waste liquid. There are two methods for precipitating the organic matter in the organic waste liquid, which can flexibly treat the organic waste liquid and improve the organic waste. Liquid treatment efficiency;

(3)粗滤:将电解后电解槽上部的有机废液通过滤芯进行粗滤,通过设置粗滤步骤,可提高电解槽内废液的过滤效率,以缩短过滤时间;(3) rough filtration: the organic waste liquid in the upper part of the electrolysis tank is subjected to rough filtration through the filter element, and by setting the rough filtration step, the filtration efficiency of the waste liquid in the electrolytic tank can be improved to shorten the filtration time;

(4)精滤:将粗滤后废液传送至过滤槽,通过过滤槽内底部的过滤膜精滤后排入清水池,经过初滤后的废液中渣滓较少,可提高精滤的效率,同时提高过滤膜的使用寿命。(4) Fine filtration: the waste liquid after rough filtration is sent to the filter tank, and then discharged into the clear water tank after fine filtration through the filter membrane at the bottom of the filter tank. efficiency, while increasing the service life of the filter membrane.

所述微电流的值为1~3安。The value of the microcurrent is 1-3 amps.

一种有机废液处理装置,包括电解槽以及与电解槽连通的过滤槽,所述电解槽上方设有电解液箱,电解槽上部的侧壁上设有废水进料管和并联在废水进料管上的浓度仪,电解槽内设有微电解器,所述微电解器包括安装在电解槽上的支撑架、安装在支撑架上的伸缩杆和设置在伸缩杆两端的电极片组,所述电极片组置于有机废液内,所述伸缩杆内设有与电极片组连接的弹簧电源线,所述支撑架上设有与弹簧电源线连接的可调变压器,所述电解槽底部设有排污管,所述电解槽的侧壁上设有与过滤槽连通的排液管,电解槽内的排液管的进料端连接有滤芯,电解槽外的排液管上设有阀门,阀门与过滤槽之间的排液管上设有反吹管,所述过滤槽内设有多层过滤膜,结合有机废液处理方法设计出包含两种处理方法的装置,可提高有机废液的处理效率。An organic waste liquid treatment device, comprising an electrolytic cell and a filter tank communicated with the electrolytic cell, an electrolyte tank is arranged above the electrolytic cell, a waste water feeding pipe is arranged on the side wall of the upper part of the electrolytic cell, and a waste water feed pipe is connected in parallel. The concentration meter on the tube, the electrolytic cell is provided with a micro-electrolyzer, and the micro-electrolyzer includes a support frame installed on the electrolytic cell, a telescopic rod installed on the support frame, and an electrode sheet set at both ends of the telescopic rod, so The electrode sheet group is placed in the organic waste liquid, the telescopic rod is provided with a spring power cord connected to the electrode sheet group, the support frame is provided with an adjustable transformer connected with the spring power cord, and the bottom of the electrolytic cell is provided with a spring power cord. A drain pipe is provided, the side wall of the electrolytic cell is provided with a drain pipe that communicates with the filter tank, the feed end of the drain pipe in the electrolytic cell is connected with a filter element, and the drain pipe outside the electrolytic cell is provided with a valve , There is a backflushing pipe on the drain pipe between the valve and the filter tank, and the filter tank is equipped with a multi-layer filter membrane. Combined with the organic waste liquid treatment method, a device including two treatment methods is designed, which can improve the organic waste liquid. processing efficiency.

所述电解液箱内设有强电解器,电解液箱底部设有连接在浓度仪后段废水进料管连接的电解液管,所述废水进料管的出口端设有混料涡轮,通过电解液箱和混料涡轮,可减少混料步骤,提高处理效率。The electrolyte tank is provided with a strong electrolyzer, the bottom of the electrolyte tank is provided with an electrolyte pipe connected to the waste water feed pipe in the rear section of the concentration meter, and the outlet end of the waste water feed pipe is provided with a mixing turbine, Electrolyte tank and mixing turbine can reduce mixing steps and improve processing efficiency.

所述电解槽顶部铰接有密封盖,通过设置密封盖,可避免电解有机废液时有机废液产生的难闻气体挥发,污染空气。A sealing cover is hinged on the top of the electrolytic cell, and by arranging the sealing cover, the unpleasant gas generated by the organic waste liquid during electrolysis of the organic waste liquid can be prevented from volatilizing and polluting the air.

所述电解槽的侧壁上加工有观察窗,通过设置观察窗,提高了工作人员对处理过程的掌控。An observation window is processed on the side wall of the electrolytic cell, and by setting the observation window, the staff's control over the treatment process is improved.

本发明具有如下效果:The present invention has the following effects:

(1)通过对有机废液进行微电解或加入电解质,使有机废液中的絮凝物增加,通过絮凝物吸附有机废液中的有机物,降低了企业的生产成本,减少了净化步骤;(1) By micro-electrolysis or adding electrolyte to the organic waste liquid, the flocs in the organic waste liquid are increased, and the organic substances in the organic waste liquid are adsorbed by the flocs, which reduces the production cost of the enterprise and reduces the purification steps;

(2)通过设置浓度仪和可调变压器,可根据有机废水的浊度设定可调变压器的电压或电流大小,以保证有机废液能正常电解;(2) By setting the concentration meter and the adjustable transformer, the voltage or current of the adjustable transformer can be set according to the turbidity of the organic waste water, so as to ensure that the organic waste liquid can be electrolyzed normally;

(3)通过设置电解液箱,可对避免直接电解有机废液时、电流过大造成有机废液燃烧或爆炸,提高了电解过程的安全性;(3) By setting the electrolyte tank, it can avoid the burning or explosion of the organic waste liquid when the organic waste liquid is directly electrolyzed and the current is too large, and the safety of the electrolysis process is improved;

(4)通过设置混料涡轮,可在有机废液传送的过程中将电解液箱内电解产生的絮状物与有机物混合,减少了后期搅拌的过程,缩短了混料时间;(4) By setting the mixing turbine, the flocs produced by electrolysis in the electrolyte tank can be mixed with the organics during the transmission of the organic waste liquid, which reduces the process of later stirring and shortens the mixing time;

(5)通过设置反吹管,可对滤芯进行反吹,以避免滤芯堵塞降低了生产效率,同时延长了滤芯的使用寿命;(5) By setting the backflushing pipe, the filter element can be backflushed, so as to avoid the blockage of the filter element and reduce the production efficiency, and at the same time prolong the service life of the filter element;

(6)通过设置观察窗,可方便地观察有机废液的沉淀过程;(6) By setting the observation window, the precipitation process of the organic waste liquid can be easily observed;

(7)通过设置伸缩杆,可根据有机废液的浓度调整电极片组之间的距离,以保证电解反应的稳定性。(7) By setting the telescopic rod, the distance between the electrode sheet groups can be adjusted according to the concentration of the organic waste liquid, so as to ensure the stability of the electrolysis reaction.

附图说明Description of drawings

图1为本发明的结构示意图。FIG. 1 is a schematic structural diagram of the present invention.

图2为本发明微电解器的结构示意图。FIG. 2 is a schematic view of the structure of the micro-electrolyzer of the present invention.

附图标记:1、电解槽;11、废水进料管;12、浓度仪;13、混料涡轮;14、排污管;15、排液管;16、密封盖;17、观察窗;18、滤芯;2、过滤槽;21、过滤膜;3、电解液箱;31、强电解器;32、电解液管;4、微电解器;41、支撑架;42、伸缩杆;43、电极片组;44、弹簧电源线;45、可调变压器;5、阀门;6、反吹管。Reference numerals: 1. Electrolytic cell; 11. Waste water feeding pipe; 12. Concentration meter; 13. Mixing turbine; 14. Sewage pipe; 15. Discharge pipe; 16. Sealing cover; Filter element; 2. Filter tank; 21. Filter membrane; 3. Electrolyte tank; 31. Strong electrolyzer; 32. Electrolyte tube; 4. Micro-electrolyzer; 41. Support frame; 42. Telescopic rod; 43. Electrode group; 44, spring power cord; 45, adjustable transformer; 5, valve; 6, blowback pipe.

具体实施方式Detailed ways

实施例1Example 1

本实施例提供的有机废液处理方法,包括以下步骤:The organic waste liquid treatment method provided by the present embodiment comprises the following steps:

(1)初滤:对pH值为3~4、常温密度大于1.0×10^3kg/m3的有机废液进行初滤,将有机废液中的悬浮物滤出。(1) Preliminary filtration: perform preliminary filtration on the organic waste liquid with a pH value of 3 to 4 and a density at room temperature greater than 1.0×10^3 kg/m 3 , and filter out the suspended solids in the organic waste liquid.

(2)电解:将有机废液引入电解槽1,并在电解槽1内的有机废液中通入1~3安直流的微电流进行电解,电极片组43阳极的材料可采用铝电极,此时微电流电解有机废液时,微电流与有机废液发生反应,产生含钙化合物,这些含钙化合物与有机废液中的有机物相互吸附,并沉淀在电解槽1底部,从而将有机废液中的有机物集中起来,以提高有机废液中的有机物的处理效率;(2) electrolysis: the organic waste liquid is introduced into the electrolytic cell 1, and the microcurrent of 1-3 ampere direct current is passed into the organic waste liquid in the electrolytic cell 1 for electrolysis, and the material of the anode of the electrode sheet group 43 can be made of aluminum electrodes, At this time, when the organic waste liquid is electrolyzed by the micro-current, the micro-current reacts with the organic waste liquid to produce calcium-containing compounds, and these calcium-containing compounds and the organic substances in the organic waste liquid are adsorbed to each other and precipitated at the bottom of the electrolytic cell 1, thereby removing the organic waste The organic matter in the liquid is concentrated to improve the treatment efficiency of the organic matter in the organic waste liquid;

(3)粗滤:有机废液电解后,产生的絮凝物沉积在电解槽1底部,此时通过滤芯18将电解槽1上部的废液滤出,用于分离有机废液中的有机物;(3) rough filtration: after the electrolysis of the organic waste liquid, the flocs produced are deposited on the bottom of the electrolytic cell 1, and the waste liquid on the top of the electrolytic cell 1 is filtered out by the filter element 18 at this time, for separating the organic matter in the organic waste liquid;

(4)精滤:将电解槽1粗滤后的废液传送至过滤槽2,通过过滤槽2内的过滤膜21对废液进行最后的精滤,以得到可达标排放的废水,并将达标排放的废水排入清水池进行检测,以检验有机废液的处理结果。(4) Fine filtration: the waste liquid after the rough filtration of the electrolytic tank 1 is sent to the filter tank 2, and the waste liquid is subjected to final fine filtration through the filter membrane 21 in the filter tank 2 to obtain the waste water that can be discharged up to the standard, and the The waste water discharged up to the standard is discharged into the clear water tank for testing to check the treatment results of the organic waste liquid.

本实施例适用于有机废液浓度较低时的处理,通入微电流电解时与有机废液产生含钙化合物,这类化合物与有机废液中的有机物相互吸附并沉淀在电解槽底部,降低了有机废液的处理成本,同时提高了有机废液的处理效率。对经过精滤后的有机废液进行检测,检测结果为pH值为6.8、密度为1.15×10^3kg/m3,达到了废水排放的标准。This embodiment is suitable for the treatment when the concentration of the organic waste liquid is low. When the micro-current is applied for electrolysis, calcium-containing compounds are produced with the organic waste liquid. Such compounds and the organic substances in the organic waste liquid are mutually adsorbed and precipitated at the bottom of the electrolytic cell, reducing the reduction of the amount of calcium. The treatment cost of organic waste liquid is improved, and the treatment efficiency of organic waste liquid is improved. The organic waste liquid after fine filtration was tested, and the test results showed that the pH value was 6.8 and the density was 1.15×10^3kg/m 3 , which met the standard of wastewater discharge.

实施例2Example 2

本实施例与实施例1基本相同,仅将步骤(2)中的电极片组43阳极的材料修改为铁电极,铁电极通入微电流后对有机废液进行电解,产生亚铁离子对有机废液中的有机物进行絮凝。This embodiment is basically the same as Embodiment 1, except that the material of the anode of the electrode sheet group 43 in step (2) is changed to iron electrodes. After the iron electrodes are charged with a microcurrent, the organic waste liquid is electrolyzed, and ferrous ions are generated to generate ferrous ions. The organic matter in the liquid is flocculated.

对经过精滤后的有机废液进行检测,检测结果为pH值为7.6、密度为1.2×10^3kg/m3,达到了废水排放的标准。The organic waste liquid after fine filtration was tested, and the test results showed that the pH value was 7.6 and the density was 1.2×10^3kg/m 3 , which met the standard of wastewater discharge.

实施例3Example 3

本实施例与实施例1基本相同,将步骤(2)中的电极片组43阳极的材料修改为不锈钢电极,同时将电解时的温度提升至80℃,不锈钢电极通入微电流后对有机废液进行电解,产生羟基基团对有机废液中的有机物进行絮凝。This example is basically the same as Example 1. The material of the anode of the electrode sheet group 43 in step (2) is changed to a stainless steel electrode, and the temperature during electrolysis is raised to 80°C. Electrolysis is performed to generate hydroxyl groups to flocculate the organic matter in the organic waste liquid.

对经过精滤后的有机废液进行检测,检测结果为pH值为7.4、密度为1.3×10^3kg/m3,达到了废水排放的标准。The organic waste liquid after fine filtration was tested, and the test results showed that the pH value was 7.4 and the density was 1.3×10^3kg/m 3 , which met the standard of wastewater discharge.

实施例4Example 4

本实施例提供的有机废液处理方法,包括以下步骤:The organic waste liquid treatment method provided by the present embodiment comprises the following steps:

(1)初滤:对pH值为3~4、常温密度大于1.0×10^3kg/m3的有机废液进行初滤,将有机废液中的悬浮物滤出(1) Primary filtration: perform primary filtration on the organic waste liquid with a pH value of 3 to 4 and a density greater than 1.0×10^3kg/m 3 at room temperature, and filter out the suspended solids in the organic waste liquid

(2)电解:将有机废液引入电解槽1,并在有机废液中加入电解液,所述电解液为强电解质中的絮状物,加入电解液时需要与电解槽1内的有机废液进行搅拌,搅拌完成后静置有机废水至有机废液中的有机物与电解液中的絮状物吸附并沉淀在电解槽1底部;(2) electrolysis: organic waste liquid is introduced into electrolytic cell 1, and electrolyte solution is added in organic waste liquid, described electrolytic solution is the floc in strong electrolyte, and organic waste in electrolytic cell 1 is required when adding electrolytic solution The liquid is stirred, and after the stirring is completed, the organic waste water is allowed to stand until the organic matter in the organic waste liquid and the flocs in the electrolyte are adsorbed and precipitated at the bottom of the electrolytic cell 1;

(3)粗滤:有机废液沉淀后,产生的絮凝物沉积在电解槽1底部,此时通过滤芯18将电解槽1上部的滤液滤出,用于分离有机废液中的有机物;(3) rough filtration: after the precipitation of the organic waste liquid, the flocs produced are deposited on the bottom of the electrolytic cell 1, and the filtrate on the top of the electrolytic cell 1 is filtered out by the filter element 18 at this time, for separating the organic matter in the organic waste liquid;

(4)精滤:将电解槽1内粗滤后的废液传送至过滤槽2,通过过滤槽2内的过滤膜21对废液进行最后的精滤,以得到可达标排放的废水,并将达标排放的废水排入清水池进行检测,以检测有机废液的处理结果。(4) fine filtration: the waste liquid after the rough filtration in the electrolytic tank 1 is sent to the filter tank 2, and the waste liquid is subjected to final fine filtration through the filter membrane 21 in the filter tank 2 to obtain the waste water that can be discharged up to the standard, and The waste water discharged up to the standard is discharged into the clean water tank for testing to check the treatment results of organic waste liquid.

本实施例适用于有机物废液浓度较高时的处理,加入电解后的电解液,因直接对浓度较高的有机废液电解容易造成爆炸或燃烧的危险,加入电解后的电解液可降低有机废液的浓度,提高了有机废液处理的安全系数。对经过精滤后的有机废液进行检测,检测结果为pH值为7.3、密度为1.0×10^3kg/m3,达到了废水排放的标准。This embodiment is suitable for the treatment when the concentration of organic waste liquid is relatively high. Adding electrolyzed electrolyte will easily cause explosion or burning danger due to the direct electrolysis of organic waste liquid with relatively high concentration. Adding electrolyzed electrolyte can reduce organic The concentration of waste liquid improves the safety factor of organic waste liquid treatment. The organic waste liquid after fine filtration was tested, and the test results showed that the pH value was 7.3 and the density was 1.0×10^3kg/m 3 , which met the standard of wastewater discharge.

实施例5Example 5

本实施例提供的有机废液处理方法,包括以下步骤The organic waste liquid treatment method provided in this embodiment includes the following steps

(1)初滤:对pH值为3~4、常温密度大于1.0×10^3kg/m3的有机废液进行初滤,将有机废液中的悬浮物滤出(1) Primary filtration: perform primary filtration on the organic waste liquid with a pH value of 3 to 4 and a density greater than 1.0×10^3kg/m 3 at room temperature, and filter out the suspended solids in the organic waste liquid

(2)电解:将有机废液引入电解槽1,并在有机废液中加入强电解质,强电解质中含有电解反应产生的絮状物,加入电解液时需要与电解槽1内的有机废液进行搅拌,然后在电解槽1内的有机废液中通入1~3安直流的微电流进行电解,微电流电解有机废液时,在有机废液中产生含钙化合物,这些含钙化合物与电解液中的絮状物相互配合将有机废液中的有机物吸附,并沉淀在电解槽1底部;(2) Electrolysis: the organic waste liquid is introduced into the electrolytic cell 1, and a strong electrolyte is added to the organic waste liquid. The strong electrolyte contains the flocs produced by the electrolysis reaction, and the organic waste liquid in the electrolytic cell 1 needs to be mixed with the organic waste liquid when adding the electrolyte. Stirring, then in the organic waste liquid in the electrolytic cell 1, a microcurrent of 1 to 3 ampere direct current is passed into the electrolysis, and when the microcurrent electrolyzes the organic waste liquid, calcium-containing compounds are produced in the organic waste liquid, and these calcium-containing compounds and The flocs in the electrolyte cooperate with each other to adsorb the organic matter in the organic waste liquid and precipitate at the bottom of the electrolytic cell 1;

(3)粗滤:有机废液沉淀后,产生的絮凝物沉积在电解槽1底部,此时通过滤芯18将电解槽1上部的滤液滤出,用于分离有机废液中的有机物;(3) rough filtration: after the precipitation of the organic waste liquid, the flocs produced are deposited on the bottom of the electrolytic cell 1, and the filtrate on the top of the electrolytic cell 1 is filtered out by the filter element 18 at this time, for separating the organic matter in the organic waste liquid;

(4)精滤:将电解槽1内粗滤后的废液传送至过滤槽2,通过过滤槽2内的过滤膜21对废液进行最后的精滤,以得到可达标排放的废水,并将达标排放的废水排入清水池进行检测,以检测有机废液的处理结果。(4) fine filtration: the waste liquid after the rough filtration in the electrolytic tank 1 is sent to the filter tank 2, and the waste liquid is subjected to final fine filtration through the filter membrane 21 in the filter tank 2 to obtain the waste water that can be discharged up to the standard, and The waste water discharged up to the standard is discharged into the clean water tank for testing to check the treatment results of organic waste liquid.

本实施例可处理浓度较高的有机废液,通过两种处理方法的结合,提高了处理效率。对经过精滤后的有机废液进行检测,检测结果为pH值为7.0、密度为1.0×10^3kg/m3,达到了清水的标准,从而达到了废水的排放标准。This embodiment can treat organic waste liquid with higher concentration, and the treatment efficiency is improved by the combination of the two treatment methods. The organic waste liquid after fine filtration is tested, and the test result is that the pH value is 7.0 and the density is 1.0×10^3kg/m 3 , which has reached the standard of clean water and thus the discharge standard of waste water.

如图1、图2所示,本发明公开的有机废液处理装置包括电解槽1以及与电解槽1连通的过滤槽2,电解槽1顶部铰接有密封盖16,电解槽1上部的侧壁上设有废水进料管11和并联在废水进料管11上的浓度仪12,电解槽1内设有微电解器4,所述微电解器4包括安装在电解槽1上的支撑架41、安装在支撑架41上的伸缩杆42和设置在伸缩杆42两端的电极片组43,所述电极片组43置于有机废液内,所述伸缩杆42内设有与电极片组43连接的弹簧电源线44,所述支撑架41上设有与弹簧电源线44连接的可调变压器45,所述浓度仪12可通过逻辑编程控制器与可调变压器45连接,用于自动控制(一般是工作人员手动调节,以便于采集各项数据),所述电解槽1底部设有排污管14,电解槽1的侧壁上加工有观察窗17,所述电解槽1上方设有电解液箱3,所述电解液箱3内设有强电解器31,电解液箱3底部设有连接在浓度仪12后段废水进料管11连接的电解液管32,所述废水进料管11的出口端设有混料涡轮13,所述电解槽1的侧壁上设有与过滤槽2连通的排液管15,电解槽1内的排液管15的进料端连接有滤芯18,电解槽1外的排液管15上设有阀门5,阀门5与过滤槽2之间的排液管15上设有反吹管6,所述过滤槽2内设有多层过滤膜21。As shown in Figures 1 and 2, the organic waste liquid treatment device disclosed in the present invention comprises an electrolytic cell 1 and a filter tank 2 communicated with the electrolytic cell 1. The top of the electrolytic cell 1 is hinged with a sealing cover 16, and the side wall of the upper part of the electrolytic cell 1 There is a waste water feed pipe 11 and a concentration meter 12 connected in parallel on the waste water feed pipe 11, and a micro-electrolyzer 4 is provided in the electrolytic cell 1, and the micro-electrolyzer 4 includes a support frame 41 installed on the electrolytic cell 1. , the telescopic rod 42 installed on the support frame 41 and the electrode sheet group 43 arranged at both ends of the telescopic rod 42, the electrode sheet group 43 is placed in the organic waste liquid, and the telescopic rod 42 is provided with the electrode sheet group 43 The connected spring power line 44, the support frame 41 is provided with an adjustable transformer 45 connected with the spring power line 44, and the concentration meter 12 can be connected with the adjustable transformer 45 through a logic programming controller for automatic control ( Generally, the staff manually adjusts to facilitate the collection of various data), the bottom of the electrolytic cell 1 is provided with a sewage pipe 14, the side wall of the electrolytic cell 1 is processed with an observation window 17, and an electrolyte solution is provided above the electrolytic cell 1 Tank 3, a strong electrolyzer 31 is provided in the electrolyte tank 3, and the bottom of the electrolyte tank 3 is provided with an electrolyte pipe 32 connected to the waste water feed pipe 11 in the rear section of the concentration meter 12, and the waste water feed pipe 11 The outlet end of the electrolytic cell 1 is provided with a mixing turbine 13, the side wall of the electrolytic cell 1 is provided with a drain pipe 15 that communicates with the filter tank 2, and the feed end of the liquid drain pipe 15 in the electrolytic cell 1 is connected with a filter element 18, The drain pipe 15 outside the electrolytic cell 1 is provided with a valve 5 , and the drain pipe 15 between the valve 5 and the filter tank 2 is provided with a blowback pipe 6 , and the filter tank 2 is provided with a multi-layer filter membrane 21 .

本发明有机废弃物处理装置的使用方法一:The use method one of the organic waste treatment device of the present invention:

通过废水进料管11将有机废液送入电解槽1,有机废液传送时浓度仪12检测有机废液的浓度,用于给工作人员提供有机废液的浓度参数,工作人员根据有机废液的浓度参数调整微电解器4上伸缩杆42的长度,以保证电极片组43之间的距离可方便地对有机废液进行微电解,电解时工作人员根据浓度仪12提供的参数控制可调变压器45的电压大小,用于控制微电解的电压及电流大小,电解产生的含钙化合物吸附有机废液中的有机物,并将有机物沉淀在电解槽1底部,随后通过滤芯18过滤废液,并通过排液管15将过滤后的废液传入过滤槽2,通过过滤槽2内的过滤膜21过滤废液后得到达标排放的废水。The organic waste liquid is fed into the electrolytic cell 1 through the waste water feeding pipe 11, and the concentration meter 12 detects the concentration of the organic waste liquid when the organic waste liquid is conveyed, which is used to provide the staff with the concentration parameters of the organic waste liquid. Adjust the length of the telescopic rod 42 on the micro-electrolyzer 4 according to the concentration parameter of the micro-electrolyzer 4 to ensure that the distance between the electrode sheet groups 43 can be easily micro-electrolyzed to the organic waste liquid. The voltage of the transformer 45 is used to control the voltage and current of the micro-electrolysis, and the calcium-containing compound produced by the electrolysis adsorbs the organic matter in the organic waste liquid, and precipitates the organic matter at the bottom of the electrolytic cell 1, and then filters the waste liquid through the filter element 18, and The filtered waste liquid is introduced into the filter tank 2 through the drain pipe 15 , and the waste liquid is filtered through the filter membrane 21 in the filter tank 2 to obtain the waste water discharged up to the standard.

本发明有机废弃物处理装置的使用方法二:Use method two of the organic waste treatment device of the present invention:

通过废水进料管11将有机废液送入电解槽1,有机废液传送之前,通过强电解器31对电解液箱3内的试剂电解,得到含有絮状物的电解质,当有机废液传送时,通过电解液管32将电解质与有机废液同时送入电解槽1内,此时废水进料管11上的混料涡轮13使有机废水与电解质均匀混合,随后电解质中的絮状物吸附有机废水中的有机物,并将有机物沉淀在电解槽1底部,随后通过滤芯18过滤废液,并通过排液管15将过滤后的废液传入过滤槽2,通过过滤槽2内的过滤膜21过滤废液后得到达标排放的废水。The organic waste liquid is sent into the electrolytic tank 1 through the waste water feeding pipe 11. Before the organic waste liquid is sent, the reagents in the electrolyte tank 3 are electrolyzed by the strong electrolyzer 31 to obtain an electrolyte containing flocs. At this time, the electrolyte and organic waste liquid are simultaneously sent into the electrolytic cell 1 through the electrolyte pipe 32. At this time, the mixing turbine 13 on the waste water feeding pipe 11 uniformly mixes the organic wastewater and the electrolyte, and then the flocs in the electrolyte are adsorbed. The organic matter in the organic waste water is deposited at the bottom of the electrolytic tank 1, then the waste liquid is filtered through the filter element 18, and the filtered waste liquid is introduced into the filter tank 2 through the drain pipe 15, and the filter membrane in the filter tank 2 is passed. 21 After filtering the waste liquid, the waste water that reaches the standard discharge is obtained.

本发明有机废弃物处理装置的使用方法三:Use method three of the organic waste treatment device of the present invention:

通过废水进料管11将有机废液送入电解槽1,有机废液传送时通过浓度仪12检测有机废液的浓度,用于给工作人员提供有机废液的浓度参数,工作人员根据有机废液的浓度参数调整微电解器4上伸缩杆42的长度,以保证电极片组43之间的距离可方便地对有机废液进行微电解,电解时工作人员根据浓度仪12提供的参数控制可调变压器45的电压大小,用于控制微电解的电压及电流大小,有机废液传送之前,通过强电解器31对电解液箱3内的试剂电解,得到含有絮状物的电解质,当有机废液传送时,通过电解液管32将电解质与有机废液同时送入电解槽1内,此时废水进料管11上的混料涡轮13使有机废水与电解质均匀混合,随后微电解器4对有机废水进行电解,使有机废液中的有机物沉淀在电解槽1底部,随后滤芯18过滤废液,并通过排液管15将过滤后的废液传入过滤槽2,通过过滤槽2内的过滤膜21过滤废液后得到达标排放的废水。The organic waste liquid is sent into the electrolytic cell 1 through the waste water feeding pipe 11, and the concentration of the organic waste liquid is detected by the concentration meter 12 during the transmission of the organic waste liquid, which is used to provide the staff with the concentration parameters of the organic waste liquid. The concentration parameter of the liquid adjusts the length of the telescopic rod 42 on the micro-electrolyzer 4 to ensure that the distance between the electrode sheet groups 43 can easily perform micro-electrolysis on the organic waste liquid. The voltage of the transformer 45 is adjusted to control the voltage and current of the micro-electrolysis. Before the organic waste liquid is sent, the reagents in the electrolyte tank 3 are electrolyzed by the strong electrolyzer 31 to obtain an electrolyte containing floccules. When the liquid is conveyed, the electrolyte and organic waste liquid are simultaneously sent into the electrolytic cell 1 through the electrolyte pipe 32. At this time, the mixing turbine 13 on the waste water feeding pipe 11 makes the organic wastewater and the electrolyte evenly mixed, and then the micro-electrolyzer 4 pairs The organic waste water is electrolyzed, so that the organic matter in the organic waste liquid is precipitated at the bottom of the electrolytic tank 1, and then the filter element 18 filters the waste liquid, and the filtered waste liquid is introduced into the filter tank 2 through the drain pipe 15, and passes through the filter tank 2. After the filter membrane 21 filters the waste liquid, the waste water that meets the standard discharge is obtained.

通过滤芯18过滤前,工作人员通过观察窗17观察有机废液是否分层。当滤芯18堵塞时,通过反吹管6和排液管15往电解槽1内吹入空气或水将堵塞滤芯18的沉淀物吹出。Before filtering through the filter element 18, the staff observes whether the organic waste liquid is layered through the observation window 17. When the filter element 18 is blocked, air or water is blown into the electrolytic cell 1 through the blowback pipe 6 and the drain pipe 15 to blow out the sediment that blocks the filter element 18 .

废液排出后,通过电解槽1底部的排污管14将沉淀后的有机物排出,用于对有机物进行回收,提高资源的利用率。After the waste liquid is discharged, the precipitated organic matter is discharged through the sewage pipe 14 at the bottom of the electrolytic cell 1 to recover the organic matter and improve the utilization rate of resources.

以上所述仅是本发明优选的实施方式,但本发明的保护范围并不局限于此,任何基于本发明所提供的技术方案和发明构思进行的改造和替换都应涵盖在本发明的保护范围内。The above are only the preferred embodiments of the present invention, but the protection scope of the present invention is not limited to this. Any modification and replacement based on the technical solutions and inventive concepts provided by the present invention should be covered by the protection scope of the present invention. Inside.

Claims (6)

1.一种有机废液处理方法,其特征在于包括以下步骤:1. a method for treating organic waste liquid, is characterized in that comprising the following steps: (1)初滤:对有机废液进行初滤,用于将有机废液中的悬浮物滤出;(1) Preliminary filtration: carry out preliminary filtration to the organic waste liquid for filtering out the suspended matter in the organic waste liquid; (2)电解:将有初滤后的机废液引入电解槽,并在电解槽内的有机废液中通入微电流进行电解至有机废液中的有机物沉淀,或在有机废液中加入电解液,加入电解液时需要将电解槽内的有机废液和电解液搅拌均匀后静置至有机废液中的有机物沉淀;(2) Electrolysis: introduce the organic waste liquid after primary filtration into the electrolytic cell, and pass a microcurrent into the organic waste liquid in the electrolytic cell to carry out electrolysis to the organic matter precipitation in the organic waste liquid, or add electrolysis to the organic waste liquid When adding the electrolyte, it is necessary to stir the organic waste liquid and the electrolyte in the electrolytic tank evenly and then let it stand to precipitate the organic matter in the organic waste liquid; (3)粗滤:将电解后电解槽上部的有机废液通过滤芯进行粗滤;(3) rough filtration: the organic waste liquid in the upper part of the electrolyzer after the electrolysis is subjected to rough filtration through the filter element; (4)精滤:将粗滤后废液传送至过滤槽,通过过滤槽内底部的过滤膜精滤后排入清水池。(4) Fine filtration: the waste liquid after rough filtration is sent to the filter tank, and then discharged into the clean water tank after fine filtration through the filter membrane at the bottom of the filter tank. 2.根据权利要求1所述的有机废液处理方法,其特征在于:所述步骤(1)中的微电流的值为1~3安。2 . The method for treating organic waste liquid according to claim 1 , wherein the value of the microcurrent in the step (1) is 1-3 A. 3 . 3.一种有机废液处理装置,其特征在于:包括电解槽以及与电解槽连通的过滤槽,所述电解槽上方设有电解液箱,电解槽上部的侧壁上设有废水进料管和并联在废水进料管上的浓度仪,电解槽内设有微电解器,所述微电解器包括安装在电解槽上的支撑架、安装在支撑架上的伸缩杆和设置在伸缩杆两端的电极片组,所述电极片组置于有机废液内,所述伸缩杆内设有与电极片组连接的弹簧电源线,所述支撑架上设有与弹簧电源线连接的可调变压器,所述电解槽底部设有排污管,所述电解槽的侧壁上设有与过滤槽连通的排液管,电解槽内的排液管的进料端连接有滤芯,电解槽外的排液管上设有阀门,阀门与过滤槽之间的排液管上设有反吹管,所述过滤槽内设有多层过滤膜。3. an organic waste liquid treatment device, it is characterized in that: comprise electrolyzer and the filter tank that communicates with electrolyzer, described electrolyzer top is provided with electrolyte tank, and the side wall of electrolyzer top is provided with waste water feed pipe And the concentration meter connected in parallel on the waste water feeding pipe, the electrolyzer is provided with a micro-electrolyzer, and the micro-electrolyzer includes a support frame installed on the electrolysis cell, a telescopic rod installed on the support frame, and two sets on the telescopic rod. The electrode sheet group is placed in the organic waste liquid, the telescopic rod is provided with a spring power cord connected to the electrode sheet group, and the support frame is provided with an adjustable transformer connected with the spring power cord , the bottom of the electrolytic cell is provided with a sewage pipe, the side wall of the electrolytic cell is provided with a liquid drain pipe that communicates with the filter tank, the feeding end of the liquid drain pipe in the electrolytic cell is connected with a filter element, and the discharge pipe outside the electrolytic cell is connected with a filter element. A valve is arranged on the liquid pipe, a backflushing pipe is arranged on the drain pipe between the valve and the filter tank, and a multi-layer filter membrane is arranged in the filter tank. 4.根据权利要求3所述的有机废液处理装置,其特征在于:所述电解液箱内设有强电解器,电解液箱底部设有连接在浓度仪后段废水进料管连接的电解液管,所述废水进料管的出口端设有混料涡轮。4. The organic waste liquid treatment device according to claim 3, characterized in that: the electrolyte tank is provided with a strong electrolyzer, and the electrolyte tank bottom is provided with an electrolysis device connected to the waste water feed pipe in the rear section of the concentration meter. A liquid pipe, the outlet end of the waste water feeding pipe is provided with a mixing turbine. 5.根据权利要求3所述的有机废液处理装置,其特征在于:所述电解槽顶部铰接有密封盖。5 . The organic waste liquid treatment device according to claim 3 , wherein a sealing cover is hinged on the top of the electrolytic cell. 6 . 6.根据权利要求3所述的有机废液处理装置,其特征在于:所述电解槽的侧壁上加工有观察窗。6 . The organic waste liquid treatment device according to claim 3 , wherein an observation window is processed on the side wall of the electrolytic cell. 7 .
CN201910389393.2A 2019-05-10 2019-05-10 A kind of organic liquid waste processing method and processing device Pending CN110040887A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110615559A (en) * 2019-10-31 2019-12-27 湖南新有爱农业有限公司 Rice deep-processing is with soaking rice effluent treatment plant
CN111573915A (en) * 2020-05-19 2020-08-25 北京泷涛环境科技有限公司 Sewage treatment device and sewage treatment system based on electrochemical oxidation and ultrafiltration
CN114683798A (en) * 2020-12-29 2022-07-01 陕西青朗万城环保科技有限公司 Air purification treatment method and control system thereof

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004097950A (en) * 2002-09-10 2004-04-02 Sanyo Electric Co Ltd Wastewater treatment apparatus and wastewater treatment system
CN2635681Y (en) * 2003-07-15 2004-08-25 上海通环医疗器械有限公司 Working voltage adjuster for electrolytic tank
CN105523668A (en) * 2015-12-04 2016-04-27 陈丽珊 PCB ammonia-nitrogen wastewater zero discharge treatment method and device thereof
CN105601002A (en) * 2015-12-29 2016-05-25 宁磊 A treatment system and method for purifying organic wastewater
CN205907066U (en) * 2016-06-16 2017-01-25 兰州交通大学 Multi -functional electrolytic device of electrolysis phenol wastewater
CN206109560U (en) * 2016-09-30 2017-04-19 广东天路新材料科技有限公司 Fused salt electrolysis groove of production rare metal and alloy
CN206570065U (en) * 2017-03-10 2017-10-20 南京大学 An electrolytic cell with adjustable plate spacing
CN206590996U (en) * 2017-03-07 2017-10-27 江苏南大生态环境建设有限公司 A kind of integration apparatus for being electrolysed cyclic regeneration advanced treatment of wastewater and reuse
CN107377612A (en) * 2017-08-30 2017-11-24 清华大学 A kind of method that electronic resistance heating in original position cooperates with repairing polluted soil and underground water
TW201803812A (en) * 2016-07-21 2018-02-01 吳凰慈 Electrolysis apparatus
CN107721040A (en) * 2017-11-29 2018-02-23 深圳市尚用来环保投资有限公司 A kind of garbage percolation liquid treating system and its method
CN207748965U (en) * 2017-10-07 2018-08-21 潍坊恒远环保水处理设备有限公司 A kind of industrial wastewater quick treatment device for reducing sewage discharge
CN208532304U (en) * 2018-07-23 2019-02-22 四川新能水处理工程有限公司 A kind of sewage-treatment plant
CN210313847U (en) * 2019-05-10 2020-04-14 四川省科源工程技术测试中心 Organic waste liquid treatment device

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004097950A (en) * 2002-09-10 2004-04-02 Sanyo Electric Co Ltd Wastewater treatment apparatus and wastewater treatment system
CN2635681Y (en) * 2003-07-15 2004-08-25 上海通环医疗器械有限公司 Working voltage adjuster for electrolytic tank
CN105523668A (en) * 2015-12-04 2016-04-27 陈丽珊 PCB ammonia-nitrogen wastewater zero discharge treatment method and device thereof
CN105601002A (en) * 2015-12-29 2016-05-25 宁磊 A treatment system and method for purifying organic wastewater
CN205907066U (en) * 2016-06-16 2017-01-25 兰州交通大学 Multi -functional electrolytic device of electrolysis phenol wastewater
TW201803812A (en) * 2016-07-21 2018-02-01 吳凰慈 Electrolysis apparatus
CN206109560U (en) * 2016-09-30 2017-04-19 广东天路新材料科技有限公司 Fused salt electrolysis groove of production rare metal and alloy
CN206590996U (en) * 2017-03-07 2017-10-27 江苏南大生态环境建设有限公司 A kind of integration apparatus for being electrolysed cyclic regeneration advanced treatment of wastewater and reuse
CN206570065U (en) * 2017-03-10 2017-10-20 南京大学 An electrolytic cell with adjustable plate spacing
CN107377612A (en) * 2017-08-30 2017-11-24 清华大学 A kind of method that electronic resistance heating in original position cooperates with repairing polluted soil and underground water
CN207748965U (en) * 2017-10-07 2018-08-21 潍坊恒远环保水处理设备有限公司 A kind of industrial wastewater quick treatment device for reducing sewage discharge
CN107721040A (en) * 2017-11-29 2018-02-23 深圳市尚用来环保投资有限公司 A kind of garbage percolation liquid treating system and its method
CN208532304U (en) * 2018-07-23 2019-02-22 四川新能水处理工程有限公司 A kind of sewage-treatment plant
CN210313847U (en) * 2019-05-10 2020-04-14 四川省科源工程技术测试中心 Organic waste liquid treatment device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110615559A (en) * 2019-10-31 2019-12-27 湖南新有爱农业有限公司 Rice deep-processing is with soaking rice effluent treatment plant
CN111573915A (en) * 2020-05-19 2020-08-25 北京泷涛环境科技有限公司 Sewage treatment device and sewage treatment system based on electrochemical oxidation and ultrafiltration
CN114683798A (en) * 2020-12-29 2022-07-01 陕西青朗万城环保科技有限公司 Air purification treatment method and control system thereof

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Application publication date: 20190723