[go: up one dir, main page]

CN105523626B - A kind of nickel-plating waste water water cleaning systems and process for purifying water - Google Patents

A kind of nickel-plating waste water water cleaning systems and process for purifying water Download PDF

Info

Publication number
CN105523626B
CN105523626B CN201610026027.7A CN201610026027A CN105523626B CN 105523626 B CN105523626 B CN 105523626B CN 201610026027 A CN201610026027 A CN 201610026027A CN 105523626 B CN105523626 B CN 105523626B
Authority
CN
China
Prior art keywords
resin
water
nickel
electrode layer
particle electrode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201610026027.7A
Other languages
Chinese (zh)
Other versions
CN105523626A (en
Inventor
冯岩
巩玉帅
于衍真
汪少华
李雪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Jinan
Original Assignee
University of Jinan
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Jinan filed Critical University of Jinan
Priority to CN201610026027.7A priority Critical patent/CN105523626B/en
Publication of CN105523626A publication Critical patent/CN105523626A/en
Application granted granted Critical
Publication of CN105523626B publication Critical patent/CN105523626B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological 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
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/16Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (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)
  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

本发明公开了一种镀镍废水净水系统及净水方法。镀镍废水净水系统的树脂型粒子电极层位于净水系统的底部,并在树脂顶部放置由钛网构成的阳极,在树脂底部放置由不锈钢孔板构成的阴极,阳极和阴极分别与外加电源的正极和负极相连,吸附性生物滤料层位于树脂型粒子电极层的上方,树脂型粒子电极层的下方与溶气配水室相连,溶气配水室内安装有曝气装置和反冲洗装置。本发明的净水方法,包括如下步骤:(1)污水进入溶气配水室;(2)气水混合(3)树脂型粒子电极处理;(4)微生物处理以及物理过滤;(5)出净水。本发明的净水系统先以树脂型粒子电极催化氧化镀镍废水中的难生物降解有机物,提高镀镍废水可生化性,再经微生物处理后排出,解决了镀镍废水难处理的问题。

The invention discloses a nickel-plating waste water purification system and a water purification method. The resin-type particle electrode layer of the nickel-plated wastewater purification system is located at the bottom of the water purification system, and an anode made of titanium mesh is placed on the top of the resin, and a cathode made of stainless steel orifice is placed at the bottom of the resin. The anode and the cathode are respectively connected to the external power supply. The positive and negative electrodes are connected, the adsorption biological filter material layer is located above the resin particle electrode layer, and the resin particle electrode layer is connected to the dissolved air water distribution chamber below, and the dissolved air water distribution chamber is equipped with an aeration device and a backwashing device. The water purification method of the present invention includes the following steps: (1) sewage enters the dissolved air water distribution chamber; (2) gas-water mixing (3) resin-type particle electrode treatment; (4) microbial treatment and physical filtration; water. The water purification system of the present invention first catalyzes and oxidizes the refractory organic matter in the nickel-plating wastewater by using the resin particle electrode to improve the biodegradability of the nickel-plating wastewater, and then discharges it after being treated by microorganisms, thereby solving the problem that the nickel-plating wastewater is difficult to handle.

Description

一种镀镍废水净水系统及净水方法A nickel-plating wastewater purification system and water purification method

技术领域technical field

本发明属于废水处理技术领域,特别是涉及一种可用于废水处理的镀镍废水净水系统和净水方法。The invention belongs to the technical field of wastewater treatment, and in particular relates to a nickel-plating wastewater purification system and a water purification method that can be used for wastewater treatment.

背景技术Background technique

镀镍工艺因具有通用性强,适用面广等特点,在工业生产中得到广泛应用,由此产生的镀镍废水也大量增加。镀镍废水是镀镍工业生产过程中产生的含金属离子和部分有机物的混合废水,如果任其自由排放,将对自然生态环境及人类健康构成严重的潜在风险。镀镍废水中含有的大量重金属离子,对动植物表现出强烈的毒性,直接排放到环境中,不仅会对生态环境造成难以修复的污染,而且有毒物质会通过食物链的富集作用,逐渐对人的健康产生危害。The nickel plating process has been widely used in industrial production because of its versatility and wide application range, and the resulting nickel plating wastewater has also increased significantly. Nickel plating wastewater is a mixed wastewater containing metal ions and some organic matter produced in the process of nickel plating industry. If it is allowed to discharge freely, it will pose serious potential risks to the natural ecological environment and human health. A large amount of heavy metal ions contained in nickel-plating wastewater show strong toxicity to animals and plants, and if they are directly discharged into the environment, it will not only cause irreparable pollution to the ecological environment, but also the toxic substances will gradually affect human beings through the enrichment of the food chain. health hazard.

随着镀镍工艺复杂程度的增加以及镀镍工艺中大量难降解有机物的使用,导致镀镍废水的处理难度也越来越大,传统的污水处理方法难以对其进行有效的处理。再加上与之相关的废水排放标准不断提高,大部分现有镀镍废水处理工艺已无法顺利使其达标排放。因此对已有镀镍废水处理工艺进行升级已经到了势在必行的阶段。With the increase in the complexity of the nickel plating process and the use of a large number of refractory organic substances in the nickel plating process, the treatment of nickel plating wastewater is becoming more and more difficult, and traditional sewage treatment methods are difficult to effectively treat it. Coupled with the continuous improvement of related wastewater discharge standards, most of the existing nickel plating wastewater treatment processes have been unable to successfully discharge them up to the standard. Therefore, it is imperative to upgrade the existing nickel plating wastewater treatment process.

本发明通过树脂型粒子电极处理技术,提高废水BOD/COD的值,使大部分难生物降解的污染物能够转化为易被微生物氧化分解的物质,之后通过吸附型生物滤料层进行生物处理,达到增强处理效果的目的,从而提高污水中污染物质的去除效率,降低设备投资,占地面积小,易于就地安装。The present invention improves the BOD/COD value of wastewater through the resin-type particle electrode treatment technology, so that most of the refractory biodegradable pollutants can be converted into substances that are easily oxidized and decomposed by microorganisms, and then biological treatment is carried out through the adsorption-type biological filter material layer, The purpose of enhancing the treatment effect is achieved, thereby improving the removal efficiency of pollutants in sewage, reducing equipment investment, occupying a small area, and being easy to install on site.

发明内容Contents of the invention

本发明的目的在于解决现有废水处理工艺对镀镍废水处理效果不佳的问题,提供了一种镀镍废水净水系统及净水方法。The purpose of the present invention is to solve the problem that the existing wastewater treatment process has poor treatment effect on nickel-plating wastewater, and provides a nickel-plating wastewater purification system and a water purification method.

为解决上述问题,本发明包括吸附型生物滤料层、树脂型粒子电极层和溶气配水室。In order to solve the above problems, the present invention includes an adsorption type biological filter material layer, a resin type particle electrode layer and a dissolved air water distribution chamber.

所述的树脂型粒子电极层,填充预处理后负载了Fe3+的强酸型阳离子交换树脂,并在树脂顶部放置由钛网构成的阴极,在树脂底部放置由不锈钢孔板构成的阳极,阳极和阴极分别与外加电源的正极和负极相连,强酸型阳离子交换树脂、阴极和阳极三部分共同组成树脂型粒子电极层。吸附性生物滤料层位于树脂型粒子电极层的上方,经树脂型粒子电极层处理后的水通过钛网从吸附型生物滤料底部进入,经微生物处理后由反应器顶部排出。The resin-type particle electrode layer is filled with strong-acid cation exchange resin loaded with Fe after pretreatment, and a cathode made of titanium mesh is placed on the top of the resin, and an anode made of stainless steel orifice is placed at the bottom of the resin. The cathode and the cathode are respectively connected to the positive and negative electrodes of the external power supply, and the strong acid type cation exchange resin, the cathode and the anode together form the resin particle electrode layer. The adsorption biological filter material layer is located above the resin particle electrode layer, and the water treated by the resin particle electrode layer enters from the bottom of the adsorption biological filter material through the titanium mesh, and is discharged from the top of the reactor after being treated by microorganisms.

所述的吸附型生物滤料层与树脂型粒子电极层由上而下串联在同一反应器中,反应器整体为圆柱型,树脂型粒子电极层装充阳离子交换树脂形成的树脂型粒子电极,高度300mm,吸附型生物滤料层装充3-5mm沸石,高度700mm,树脂型粒子电极层和吸附型生物滤料层直径形同。The adsorption-type biological filter material layer and the resin-type particle electrode layer are connected in series in the same reactor from top to bottom. The reactor is a cylindrical shape as a whole, and the resin-type particle electrode layer is filled with a resin-type particle electrode formed by cation exchange resin. The height is 300mm, the adsorption type biological filter material layer is filled with 3-5mm zeolite, the height is 700mm, the diameter of the resin particle electrode layer and the adsorption type biological filter material layer are the same.

所述的溶气配水室安装有污水管、反冲洗进水管、曝气管和曝气盘,反冲洗水泵和反冲洗进水管连接,空气压缩机和曝气管连接,曝气盘安装在曝气管上。The dissolved air water distribution room is equipped with a sewage pipe, a backwash water inlet pipe, an aeration pipe and an aeration pan, the backwash water pump is connected to the backwash water inlet pipe, the air compressor is connected to the aeration pipe, and the aeration pan is installed on the on the trachea.

一种采用上述所述的一种镀镍废水净水方法,包括如下步骤:(1)高位水箱内的污水经过计量泵计量,进入溶气配水室;(2)向曝气盘通入压缩空气,控制汽水体积比为4:1到2:1,空气和水在溶气配水室内充分混合(3)溶气配水室内的空气和水通过不锈钢孔板进入树脂型粒子电极层;(4)在树脂型粒子电极层的两端的钛网和不锈钢孔板通过阳极线、阴极线与直流电源的正极和负极相连,为树脂型粒子电极层提供所需的电场;(5)污水和空气经过钛网进入吸附型生物滤料层;(6)经吸附型生物滤料层处理后的水经出水管排出;(7)运行一段时间后对镀镍废水净水系统进行反冲洗,先气洗3分钟,然后同时水洗和气洗5分钟,再水洗8分钟。A method of purifying nickel-plating wastewater as described above, comprising the following steps: (1) The sewage in the high-level water tank is metered by a metering pump and enters the dissolved air water distribution chamber; (2) The compressed air is fed into the aeration pan , control the volume ratio of soda to water from 4:1 to 2:1, and the air and water are fully mixed in the dissolved air water distribution chamber (3) The air and water in the dissolved air water distribution chamber enter the resin particle electrode layer through the stainless steel orifice plate; (4) in the The titanium mesh and stainless steel orifice plate at both ends of the resin-type particle electrode layer are connected to the positive and negative electrodes of the DC power supply through the anode wire and the cathode wire to provide the required electric field for the resin-type particle electrode layer; (5) Sewage and air pass through the titanium mesh Enter the adsorption-type biological filter layer; (6) The water treated by the adsorption-type biological filter layer is discharged through the outlet pipe; (7) Backwash the nickel-plating wastewater purification system after running for a period of time, and first air wash for 3 minutes , and then wash with water and air for 5 minutes at the same time, and then wash with water for 8 minutes.

本发明的有益效果:在树脂型粒子电极的作用下提高废水BOD/COD的值,增加其可生化性,然后通过生物处理去除废水中的污染物,从而提高镀镍废水COD的去除率,并且可以有效去除废水中的重金属。Beneficial effect of the present invention: under the effect of resin type particle electrode, increase the value of waste water BOD/COD, increase its biodegradability, then remove the pollutant in waste water by biological treatment, thereby improve the removal rate of COD of nickel plating waste water, and Can effectively remove heavy metals in wastewater.

附图说明Description of drawings

图1为本发明一种镀镍废水净水系统示意图,结合本图做进一步的说明。Fig. 1 is a schematic diagram of a nickel-plating wastewater purification system according to the present invention, which will be further described in conjunction with this figure.

附图1为本发明的流程示意图。Accompanying drawing 1 is the schematic flow chart of the present invention.

图1中: 1 直流电源; 2 阳极线; 3 阴极线; 4树脂型粒子电极层; 5 吸附型生物滤料层; 6 反冲洗进水管; 7 空气压缩机; 8 反冲洗进水; 9 反冲洗水泵; 10 进水计量泵; 11 进水蠕动泵; 12 曝气管; 13 溶气配水室; 14 出水管; 15 取水(料)样口; 16污水箱; 17 不锈钢孔板电极; 18 钛网; 19 曝气盘; 20 污水管。In Fig. 1: 1. DC power supply; 2. Anode line; 3. Cathode line; 4. Resin type particle electrode layer; Rinsing water pump; 10 Water inlet metering pump; 11 Water inlet peristaltic pump; 12 Aeration pipe; 13 Dissolved air distribution chamber; 14 Water outlet pipe; 15 Water (material) sampling port; net; 19 aeration pan; 20 sewage pipe.

具体实施方式Detailed ways

实施例一:Embodiment one:

附图为本发明的一种具体实施例,该实施例包括高位水箱16中的污水通过污水计量泵10经污水管20进入溶气配水室13,溶气配水室13设有曝气盘19、曝气管12,曝气盘19通过曝气管12与空气压缩机7相连,组成曝气系统,为树脂型粒子电极和微生物提供所需氧气,反冲洗进水管6与反冲洗水泵9相连,污水在溶气配水室13内与空气充分混合后经过不锈钢孔板电极17进入树脂型粒子电极层4内,树脂型粒子电极层4外部有直流电源1,直流电源1通过阳极线2、阴极线3分别和树脂型粒子电极层4内的钛网18、不锈钢孔板电极17连接,在强酸型阳离子交换树脂区域产生电场,使树脂颗粒形成树脂型粒子电极,经树脂型粒子电极层4处理过的水经过钛网18进入吸附型生物滤料层5,污水经吸附型生物滤料层5处理后通过出水管14排出,在吸附性生物滤料外部沿竖直方向等距分布有取水(料)样口15,以便随时观测吸附型生物滤料层5不同位置水质的变化。Accompanying drawing is a kind of specific embodiment of the present invention, and this embodiment comprises that the sewage in the elevated water tank 16 enters the dissolved air water distribution chamber 13 through the sewage pipe 20 through the sewage metering pump 10, and the dissolved air water distribution chamber 13 is provided with an aeration pan 19, The aeration pipe 12 and the aeration disc 19 are connected with the air compressor 7 through the aeration pipe 12 to form an aeration system to provide the required oxygen for the resin particle electrode and microorganisms, and the backwash water inlet pipe 6 is connected with the backwash water pump 9, The sewage is fully mixed with air in the dissolved air water distribution chamber 13, and then enters the resin-type particle electrode layer 4 through the stainless steel orifice electrode 17. There is a DC power supply 1 outside the resin-type particle electrode layer 4, and the DC power supply 1 passes through the anode wire 2 and the cathode wire. 3 Connect with the titanium mesh 18 and the stainless steel orifice plate electrode 17 in the resin particle electrode layer 4 respectively, generate an electric field in the region of the strong acid cation exchange resin, and make the resin particles form a resin particle electrode, which is treated by the resin particle electrode layer 4 The water enters the adsorption-type biological filter material layer 5 through the titanium mesh 18, and the sewage is discharged through the outlet pipe 14 after being treated by the adsorption-type biological filter material layer 5. ) sample port 15, so as to observe the change of water quality at different positions of the adsorption type biological filter material layer 5 at any time.

将高位水箱16中的污水通过污水计量泵10经污水管20进入溶气配水室13,溶气配水室设有曝气盘19、曝气管12,曝气盘19通过曝气管12与空气压缩机7相连,组成曝气系统,为树脂型粒子电极和微生物提供所需氧气,污水在溶气配水室13内与空气充分混合后经过不锈钢孔板电极17进入树脂型粒子电极层4内,树脂型粒子电极层所用的填料为经过预处理的强酸型阳离子交换树脂,高300mm,经树脂型粒子电极层4处理过的水经过钛网18进入吸附型生物滤料层5,吸附型生物滤料层填充沸石,高700mm,污水经吸附型生物滤料层5处理后通过出水管14排出,水损增大到一定程度后,需要对镀镍废水净水系统进行反冲洗,反冲洗时先停止污水流入后,由空气压缩机7进行气洗,然后打开反冲洗水泵9加压对镀镍废水净水系统进行气水联合冲洗,之后关闭空气压缩机7,再用反冲洗水泵9加压对镀镍废水净水系统进行水洗,反冲洗的水经出水管14排出。The sewage in the high-level water tank 16 enters the dissolved air water distribution chamber 13 through the sewage metering pump 10 through the sewage pipe 20. The dissolved air water distribution chamber is provided with an aeration pan 19 and an aeration pipe 12. The compressors 7 are connected to form an aeration system to provide the required oxygen for the resin-type particle electrodes and microorganisms. The sewage is fully mixed with air in the dissolved air water distribution chamber 13 and then enters the resin-type particle electrode layer 4 through the stainless steel orifice electrode 17. The filler used in the resin-type particle electrode layer is pretreated strong-acid cation exchange resin with a height of 300mm. The water treated by the resin-type particle electrode layer 4 enters the adsorption-type biological filter material layer 5 through the titanium mesh 18, and the adsorption-type biological filter The material layer is filled with zeolite, with a height of 700 mm. After the sewage is treated by the adsorption type biological filter material layer 5, it is discharged through the outlet pipe 14. After the water loss increases to a certain extent, it is necessary to backwash the nickel-plating wastewater purification system. After the inflow of sewage is stopped, the air compressor 7 is used for air washing, and then the backwash water pump 9 is turned on to pressurize the nickel-plating wastewater purification system for combined air and water flushing, and then the air compressor 7 is turned off, and the backwash water pump 9 is used for pressurization The nickel-plating waste water purification system is washed with water, and the backwashed water is discharged through the outlet pipe 14.

采用上述一种镀镍废水净水方法包括如下步骤:(1)进水水力负荷为6m3/m2·h,经过计量泵10计量,进入溶气配水室13;(2)向曝气盘19通入压缩空气,空气压缩机7压力0.3Mpa,气水体积比为4:1,空气和水在溶气配水室内充分混合(3)溶气配水室13内的空气和水通过不锈钢孔板电极17进入树脂型粒子电极层4;(4)在树脂型粒子电极层4的两端的不锈钢孔板电极17和钛网18通过阴极线3、阳极线2与直流电源1的正极和负极相连,为树脂型粒子电极层4提供所需的电场;(5)污水和空气经过钛网18进入吸附型生物滤料层5;(6)经吸附型生物滤料层5处理后的水经出水管14排出;(7)运行一段时间后对镀镍废水净水系统进行反冲洗,先气洗3分钟,然后同时水洗和气洗5分钟,再水洗8分钟。The above-mentioned method for purifying nickel-plating wastewater includes the following steps: (1) The hydraulic load of the incoming water is 6m 3 /m 2 ·h, metered by the metering pump 10, and then enters the dissolved air distribution chamber 13; 19 is fed with compressed air, the pressure of the air compressor 7 is 0.3Mpa, the volume ratio of air to water is 4:1, and the air and water are fully mixed in the dissolved air water distribution chamber (3) The air and water in the dissolved air water distribution chamber 13 pass through the stainless steel orifice plate The electrode 17 enters the resin-type particle electrode layer 4; (4) the stainless steel orifice electrode 17 and the titanium mesh 18 at both ends of the resin-type particle electrode layer 4 are connected to the positive pole and the negative pole of the DC power supply 1 through the cathode line 3 and the anode line 2, Provide the required electric field for the resin-type particle electrode layer 4; (5) Sewage and air enter the adsorption-type biological filter material layer 5 through the titanium mesh 18; (6) The water treated by the adsorption-type biological filter material layer 5 passes through the outlet pipe 14 discharge; (7) Backwash the nickel-plating wastewater purification system after running for a period of time, first air wash for 3 minutes, then water wash and air wash for 5 minutes at the same time, and then water wash for 8 minutes.

实施例二:Embodiment two:

本具体实施例的镀镍废水净水系统与具体实施例一的镀镍废水净水系统相同。The nickel-plating wastewater purification system in this embodiment is the same as the nickel-plating wastewater purification system in Embodiment 1.

本净水方法与具体实施例一净水方法区别在于:曝气的气水体积比为3:1。The difference between this water purification method and the water purification method in Embodiment 1 is that the air-to-water volume ratio of the aeration is 3:1.

实施例三:Embodiment three:

本具体实施例的镀镍废水净水系统与具体实施例一的镀镍废水净水系统相同。The nickel-plating wastewater purification system in this embodiment is the same as the nickel-plating wastewater purification system in Embodiment 1.

本净水方法与具体实施例一净水方法区别在于:曝气的气水体积比为2:1。The difference between this water purification method and the specific embodiment 1 water purification method is that the air-to-water volume ratio of the aeration is 2:1.

Claims (1)

1. a kind of nickel-plating waste water water cleaning systems, it is characterised in that:Including Rong Qi distributing water room(13), resin type granule electrode layer(4)、 The absorbent-type biological filter bed of material(5), resin type granule electrode layer(4)Resin cation type particle of the filling with ion exchange Electrode, the absorbent-type biological filter bed of material(5)It is filled with zeolite, Rong Qi distributing water room(13), resin type granule electrode layer(4), absorbent-type The biological filter bed of material(5)Series connection is combined from the bottom to top in a reactor;Wherein resin type granule electrode layer(4)Outside is connected to directly Galvanic electricity source(1), DC power supply passes through anode line(2), cathode line(3)Respectively with resin type granule electrode layer(4)Interior titanium net (18), stainless steel plate electrode(17)It is connected, Rong Qi distributing water room is equipped with aeration plate(19), aeration tube(12), backwash water inlet pipe (6), sewage pipe(20), aeration tube(12)And air compressor(7)Connection backwashes water inlet pipe(6)And backwash pump(9)Even It connects, resin type granule electrode layer(4)Used resin is obtained after pretreatment by common strongly acidic cation-exchange , preprocess method is as follows, and first common strongly acidic cation-exchange is cleaned with deionized water, then cleans three with acetone It is cleaned to four times, then with deionized water, reaches deimpurity purpose, afterwards by cleaned strongly acidic cation-exchange With resin volume:Liquor capacity is 1:10 ratio is put into FeCl3When immersion 24 is small in solution, to reach load Fe3+Purpose, Finally having loaded Fe3+The strongly acidic cation-exchange of ion is from FeCl3It takes out in solution, is cleaned again with deionized water It is put into afterwards in the environment that temperature is 373K and dries the pretreatment that can be completed to resin.
CN201610026027.7A 2016-01-15 2016-01-15 A kind of nickel-plating waste water water cleaning systems and process for purifying water Expired - Fee Related CN105523626B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610026027.7A CN105523626B (en) 2016-01-15 2016-01-15 A kind of nickel-plating waste water water cleaning systems and process for purifying water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610026027.7A CN105523626B (en) 2016-01-15 2016-01-15 A kind of nickel-plating waste water water cleaning systems and process for purifying water

Publications (2)

Publication Number Publication Date
CN105523626A CN105523626A (en) 2016-04-27
CN105523626B true CN105523626B (en) 2018-05-22

Family

ID=55766208

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610026027.7A Expired - Fee Related CN105523626B (en) 2016-01-15 2016-01-15 A kind of nickel-plating waste water water cleaning systems and process for purifying water

Country Status (1)

Country Link
CN (1) CN105523626B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107619091A (en) * 2017-09-26 2018-01-23 哈尔滨工业大学 A kind of method removed the device of removing heavy metals and hardly degraded organic substance and removing heavy metals and hardly degraded organic substance are removed using the device

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006095466A (en) * 2004-09-30 2006-04-13 Hitachi Housetec Co Ltd Electrolyzer, purifying tank having the electrolyzer and electrolytic method
CN104118966B (en) * 2014-07-03 2016-01-20 济南大学 The three-dimensional electric biological coupling water cleaning systems of a kind of air water anisotropic flow and process for purifying water
CN104118931B (en) * 2014-07-03 2016-06-22 济南大学 A kind of electricity biological coupling water cleaning systems and process for purifying water
CN104118933B (en) * 2014-07-03 2016-04-20 济南大学 A kind of three-dimensional electric biological coupling water cleaning systems and process for purifying water

Also Published As

Publication number Publication date
CN105523626A (en) 2016-04-27

Similar Documents

Publication Publication Date Title
CN104118933B (en) A kind of three-dimensional electric biological coupling water cleaning systems and process for purifying water
CN105502838B (en) A kind of copper plating wastewater water cleaning systems and process for purifying water
CN203904137U (en) Cold and hot magnetizing water purification faucet
CN204824456U (en) Remove organic matter removal's filter
CN204111517U (en) The three-dimensional electric biological coupling reactor of a kind of air water anisotropic flow
CN104118965B (en) A kind of anaerobic-aerobic three-dimensional electro-catalysis coupling water cleaning systems and process for purifying water
CN212864409U (en) Water denitrification adsorption dephosphorization deep purification system
CN105565605B (en) A kind of chromium plating wastewater cleaning system and purification method
CN105523626B (en) A kind of nickel-plating waste water water cleaning systems and process for purifying water
CN105565604B (en) A kind of plating iron waste water water cleaning systems and process for purifying water
CN101955301A (en) Method and equipment for treating micropollution raw water based on biological bamboo charcoal contact oxidation method
CN105541034B (en) A kind of galvanized liquid waste water cleaning systems and process for purifying water
CN203999226U (en) A kind of printed-wiring board (PWB) Cleaning Wastewater integrated synthesis handler
CN105668923B (en) A kind of tin plating waste water water cleaning systems and process for purifying water
CN104129885B (en) A kind of to upper reaches electricity biological coupling water cleaning systems and process for purifying water
CN206447741U (en) A kind of reclaimed water treatment equipment
CN204508999U (en) A kind of combined type Water treatment sterilizing device
CN104118939B (en) An anaerobic-aerobic electrocatalytic coupled water purification system and water purification method
CN205313290U (en) Cooling circulating water treatment system that can reequip on line
CN109095726A (en) A kind of leather waste water intermediate water reuse system
CN104118967B (en) A kind of air water anisotropic flow electricity biological coupling water cleaning systems and process for purifying water
CN104118932B (en) A kind of air water anisotropic flow magnetic biofiltration water cleaning systems and process for purifying water
CN107459109A (en) The devices and methods therefor of removing heavy metals and hardly degraded organic substance is synchronously removed in a kind of air water anisotropic flow three-dimensional electro-catalysis
CN204281523U (en) Integrated slaughterhouse wastewater treatment equipment
CN105481082B (en) A kind of lead plating waste water water cleaning systems and process for purifying water

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180522

Termination date: 20210115

CF01 Termination of patent right due to non-payment of annual fee