CN1884631A - Method and device for cleaning organic matter using electrochemical method - Google Patents

Method and device for cleaning organic matter using electrochemical method Download PDF

Info

Publication number
CN1884631A
CN1884631A CN 200610013851 CN200610013851A CN1884631A CN 1884631 A CN1884631 A CN 1884631A CN 200610013851 CN200610013851 CN 200610013851 CN 200610013851 A CN200610013851 A CN 200610013851A CN 1884631 A CN1884631 A CN 1884631A
Authority
CN
China
Prior art keywords
cleaning
electrochemical
compartment
electrolytic cell
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.)
Pending
Application number
CN 200610013851
Other languages
Chinese (zh)
Inventor
常明
潘鹏
曲长庆
孙伟
周志刚
高宝红
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.)
Tianjin University of Technology
Original Assignee
Tianjin University of Technology
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 Tianjin University of Technology filed Critical Tianjin University of Technology
Priority to CN 200610013851 priority Critical patent/CN1884631A/en
Publication of CN1884631A publication Critical patent/CN1884631A/en
Pending legal-status Critical Current

Links

Landscapes

  • Cleaning Or Drying Semiconductors (AREA)

Abstract

本发明公开了一种利用电化学方法清洗有机物的方法与清洗装置。其特征在于利用金刚石膜电极作阳极,在电流密度100-5000Am-2范围之间,进行电化学方法清洗有机物。本发明充分利用金刚石膜电极在电化学氧化技术上的优势,使用金刚石膜电极产生氢氧自由基、氧自由基等强氧化粒子可进行有机清洗,例如:用来清洗光刻胶剥离半导体器件避免了传统的湿式工艺中的一定含量的重金属、碱金属元素,能达到器件设计的要求;用来进行活性炭再生,可以大大降低成本,而且不会造成环境污染。本发明利用金刚石膜电极进行有机清洗的设备简单,便于操作,并且不会产生二次污染。耗能少,满足低成本制造的要求以及对环境无害的要求。The invention discloses a method and a cleaning device for cleaning organic matter by using an electrochemical method. The method is characterized in that the diamond membrane electrode is used as an anode, and the organic matter is cleaned electrochemically in the range of current density 100-5000Am -2 . The invention makes full use of the advantages of the diamond film electrode in electrochemical oxidation technology, and uses the diamond film electrode to generate strong oxidizing particles such as hydroxyl radicals and oxygen free radicals, which can be used for organic cleaning, for example: for cleaning photoresist and stripping semiconductor devices to avoid A certain amount of heavy metals and alkali metal elements in the traditional wet process can be eliminated, which can meet the requirements of device design; it can be used for activated carbon regeneration, which can greatly reduce the cost and will not cause environmental pollution. The invention utilizes the diamond membrane electrode for organic cleaning with simple equipment, easy operation and no secondary pollution. It consumes less energy and meets the requirements of low-cost manufacturing and environmental protection.

Description

利用电化学方法清洗有机物的方法与装置Method and device for cleaning organic matter by electrochemical method

【技术领域】【Technical field】

本发明涉及电化学氧化领域,特别是一种利用电化学方法清洗有机物的方法与装置。The invention relates to the field of electrochemical oxidation, in particular to a method and a device for cleaning organic matter by using an electrochemical method.

【背景技术】【Background technique】

高级氧化处理(AOP)技术被广泛用于降解或分解有机物,特别是难降解的有机污染物。目前,电化学氧化处理对工业废水的处理扮演着十分重要的角色,氧化过程在降低有毒污染方面越来越受到人们的关注。与此同时,用电化学氧化方法处理半导体器件上的光刻胶剥离以及活性炭再生也越来越受到人们的重视。Advanced oxidation processing (AOP) technology is widely used to degrade or decompose organic matter, especially refractory organic pollutants. At present, electrochemical oxidation treatment plays a very important role in the treatment of industrial wastewater, and the oxidation process has attracted more and more attention in reducing toxic pollution. At the same time, the use of electrochemical oxidation to treat photoresist stripping and activated carbon regeneration on semiconductor devices has also attracted more and more attention.

半导体器件制造工艺中,光刻胶剥离一般采用等离子灰化,以及湿式工艺。在大多数情况下,湿式清洗是在灰化之后进行,用来清除等离子工艺导致的有机物或聚合物残留。湿式清洗使用的溶液一般是SPM-APM的混合物,其中SPM溶液是硫酸(H2SO4)和过氧化氢(H2O2)的混合物,APM溶液是氢氧化铵、过氧化氢和水的混合物。这种传统的化学清洗试剂SPM和APM都含有金属离子杂质,它们对新式栅结构的电学性能有负面影响;而且,对于清洗试剂SPM和APM,若要保证清洗效率和器件电学性能,就要求它们是一次性使用,使清洗成本很高;此外,传统化学试剂的使用和水的消耗对环境造成不良影响。In the semiconductor device manufacturing process, photoresist stripping generally adopts plasma ashing and wet process. In most cases, wet cleaning is performed after ashing to remove organic or polymer residues from the plasma process. The solution used for wet cleaning is generally a mixture of SPM-APM, where the SPM solution is a mixture of sulfuric acid (H 2 SO 4 ) and hydrogen peroxide (H 2 O 2 ), and the APM solution is a mixture of ammonium hydroxide, hydrogen peroxide and water. mixture. Both the traditional chemical cleaning reagents SPM and APM contain metal ion impurities, which have a negative impact on the electrical properties of the new gate structure; It is disposable, making the cleaning cost very high; in addition, the use of traditional chemical reagents and water consumption have a negative impact on the environment.

活性炭是一种无毒无味,具有发达细孔结构和巨大比表面积的优良吸附剂。现有技术中大量使用活性炭吸附法处理城市饮用水和工业废水,二硫化碳废水处理,以及炼油废水、炸药废水、印染废水、化工废水和电镀废水处理等方面。随着活性炭的应用范围日趋广泛,活性炭的回收开始得到了人们的重视。如果用过的活性炭无法回收,除了每吨废水的处理费用将会增加外,还会对环境造成二次污染。因此,活性炭的再生具有格外重要的意义。传统活性炭再生方法包括热再生法、生物再生法等活性炭再生的传统方法,同时目前新兴的活性炭再生技术有、超临界流体法、催化湿式氧化法和超声波法。Activated carbon is a non-toxic, odorless, excellent adsorbent with a well-developed pore structure and a large specific surface area. In the prior art, a large number of activated carbon adsorption methods are used to treat urban drinking water and industrial wastewater, carbon disulfide wastewater treatment, and oil refining wastewater, explosive wastewater, printing and dyeing wastewater, chemical wastewater and electroplating wastewater treatment. With the widening of the application range of activated carbon, the recovery of activated carbon has begun to get people's attention. If the used activated carbon cannot be recycled, in addition to increasing the treatment cost per ton of wastewater, it will also cause secondary pollution to the environment. Therefore, the regeneration of activated carbon is of great significance. Traditional activated carbon regeneration methods include thermal regeneration, biological regeneration and other traditional methods of activated carbon regeneration. At the same time, emerging activated carbon regeneration technologies include supercritical fluid method, catalytic wet oxidation method and ultrasonic method.

【发明内容】【Content of invention】

本发明的目的是为了解决现有技术的问题,而提供一种利用电化学方法清洗有机物的方法与装置,该方法利用金刚石膜电极在电化学氧化上的优势,用电解液直接清洗待清洗对象表面的有机物,效果明显优于其它应用于电化学水处理中的电极。The purpose of the present invention is to solve the problems of the prior art, and provide a method and device for cleaning organic matter by electrochemical method. The method utilizes the advantages of diamond film electrode in electrochemical oxidation, and directly cleans the object to be cleaned with electrolyte The organic matter on the surface is significantly better than other electrodes used in electrochemical water treatment.

本发明为实现发明目的公开了一种利用电化学方法清洗有机物的方法。其特征在于将含有有机物的清洗对象置于电解液中;利用金刚石膜电极作阳极,在电流密度100-5000Am-2范围之间,电化学氧化水中羟基(OH-)生成羟基自由基(OH·)氧自由基(O·)、臭氧(O3)、以及过氧化氢(H2O2)。To realize the purpose of the invention, the invention discloses a method for cleaning organic matter by using an electrochemical method. It is characterized in that the cleaning object containing organic matter is placed in the electrolyte; the diamond film electrode is used as the anode, and the hydroxyl group (OH - ) in the water is electrochemically oxidized in the range of current density 100-5000Am -2 to generate hydroxyl radical (OH· ) oxygen radicals (O·), ozone (O 3 ), and hydrogen peroxide (H 2 O 2 ).

本发明还公开了一种专用于利用电化学方法清洗有机物方法的电化学清洗装置,包括电解池、电极、离子膜,其特征在于所说的电解池是单厢电解池或是双厢、多厢电解池,双厢和多厢电解池的电解槽中间用离子膜间隔;所说的电极有一组或多组,每组电极组由阳极-金刚石膜电极和阴极-普通金属电极构成,相邻的阳极和阴极两电极间距为0.5-50mm;同时利用机械方式实现电解液的扰动。The invention also discloses an electrochemical cleaning device specially used for cleaning organic matter by electrochemical methods, including an electrolytic cell, an electrode, and an ion membrane. Compartment electrolytic cells, double-compartment and multi-compartment electrolytic cells are separated by ionic membranes; the electrodes have one or more groups, and each group of electrodes consists of anode-diamond film electrodes and cathode-common metal electrodes, adjacent to each other. The distance between the anode and the cathode is 0.5-50mm; at the same time, the disturbance of the electrolyte is realized by mechanical means.

本发明充分利用了金刚石膜电极在电化学氧化技术上的优势,发挥了金刚石膜电极的应用潜力。使用金刚石膜电极产生氢氧自由基、氧自由基等氧化粒子可进行有机清洗,例如:用来清洗光刻胶剥离半导体器件避免了传统的湿式工艺中的一定含量的重金属、碱金属元素,能达到器件设计的要求;用来进行活性炭再生,可以大大降低成本,而且不会造成环境污染。本发明利用金刚石膜电极进行有机清洗的设备简单,便于操作,并且不会产生二次污染。耗能少,满足低成本制造的要求以及对环境无害的要求。The invention fully utilizes the advantages of the diamond film electrode in the electrochemical oxidation technology, and exerts the application potential of the diamond film electrode. The use of diamond film electrodes to generate oxidized particles such as hydroxyl radicals and oxygen radicals can be used for organic cleaning, for example: used to clean photoresists and strip semiconductor devices, avoiding a certain amount of heavy metals and alkali metal elements in traditional wet processes, and can Meet the requirements of device design; used for activated carbon regeneration, can greatly reduce the cost, and will not cause environmental pollution. The invention utilizes the diamond membrane electrode for organic cleaning with simple equipment, easy operation and no secondary pollution. It consumes less energy and meets the requirements of low-cost manufacturing and environmental protection.

【附图说明】【Description of drawings】

图1电化学清洗装置示意图。Figure 1 Schematic diagram of the electrochemical cleaning device.

图中:1.阳极;2.阴极;3.水泵;4.容器;5.流量计;6.电源。In the figure: 1. Anode; 2. Cathode; 3. Water pump; 4. Container; 5. Flow meter; 6. Power supply.

【具体实施方式】【Detailed ways】

本发明利用电化学方法清洗有机物的方法,将清洗对象置于电解液中,利用金刚石膜电极作阳极,在电流密度100-5000Am-2范围之间,电化学氧化水中羟基(OH-)生成羟基自由基(OH·)氧自由基(O·)、臭氧(O3)、以及过氧化氢(H2O2)。The present invention uses an electrochemical method to clean organic matter. The cleaning object is placed in an electrolyte, and a diamond film electrode is used as an anode to electrochemically oxidize hydroxyl (OH - ) in water to generate hydroxyl in the range of current density 100-5000Am -2 Free radicals (OH·) oxygen radicals (O·), ozone (O 3 ), and hydrogen peroxide (H 2 O 2 ).

本发明的电化学清洗装置由电解池、电极、离子膜、流量计5、电源6等组成。其电解池是单厢电解池也可以是双厢或多厢电解池,双厢和多厢电解池的电解槽中间用离子膜将阴极槽和阳极槽隔开。所说的电极可以有一组或多组,每组电极组由阳极-金刚石膜电极和阴极-普通金属电极构成,相邻的阳极1和阴极2两电极间距为0.5-50mm,将电极固定在处理槽中。多组电极组的联接可以并联也可以串联。为提高清洗效率,可通过设置水泵3或搅拌器的方式实现电解液的扰动或循环。The electrochemical cleaning device of the present invention is composed of an electrolytic cell, an electrode, an ion membrane, a flow meter 5, a power source 6 and the like. The electrolytic cell is a single-compartment electrolytic cell or a double-compartment or multi-compartment electrolytic cell. The cathode tank and the anode tank are separated by an ionic membrane in the middle of the electrolytic cells of the double-compartment and multi-compartment electrolytic cells. Said electrodes can have one or more groups, each electrode group is composed of anode-diamond film electrode and cathode-ordinary metal electrode, the distance between adjacent anode 1 and cathode 2 electrodes is 0.5-50mm, and the electrodes are fixed in the in the slot. The connection of multiple sets of electrode groups can be connected in parallel or in series. In order to improve the cleaning efficiency, the disturbance or circulation of the electrolyte can be realized by setting the water pump 3 or the agitator.

为便于清洗某些清洗对象或为大量清洗清洗对象方便,电解池也可通过循环管路和循环泵连接一个清洗对象容器4。即将清洗对象置于容器,通过循环管路将电解液引入清洗容器,并可不断与电解池中的电解液循环。例如,容器用于盛装有机物污染活性炭,进行活性炭再生。当电解池是双厢或多厢电解池时,循环管路与阳极槽相通。For the convenience of cleaning certain cleaning objects or for cleaning a large number of cleaning objects, the electrolytic cell can also be connected to a cleaning object container 4 through a circulation pipeline and a circulation pump. That is to say, the cleaning object is placed in the container, and the electrolyte is introduced into the cleaning container through the circulation pipeline, and it can continuously circulate with the electrolyte in the electrolytic cell. For example, the container is used to contain the activated carbon polluted by organic matter, and the activated carbon is regenerated. When the electrolytic cell is a double-compartment or multi-compartment electrolytic cell, the circulation pipeline communicates with the anode tank.

本发明可以是对光刻胶剥离半导体器件作为清洗对象进行有机清洗。将需进行有机清洗的器件置入单厢电解池中,如果是双厢或多厢电解池,置入阳极槽中。电极组通直流电电解水,通过控制电流的大小来控制清洗效率。电流密度越大效率越高,电流密度范围在100-5000Am-2之间。The present invention can perform organic cleaning on the photoresist stripped semiconductor device as the cleaning object. Place the device to be cleaned organically into the single-compartment electrolytic cell, or into the anode tank if it is a double-compartment or multi-compartment electrolytic cell. The electrode group electrolyzes water through direct current, and the cleaning efficiency is controlled by controlling the magnitude of the current. The higher the current density, the higher the efficiency, and the current density range is between 100-5000Am -2 .

本发明也可以是对有机物污染的活性炭作为清洗对象进行活性炭再生清洗。利用单厢或多厢电解池处理器电解水,利用水泵实现处理器与活性炭容器间水的循环。电流密度越大处理效率越高,电流密度范围在100-5000Am-2之间。In the present invention, activated carbon polluted by organic substances can also be used as the cleaning object to perform activated carbon regeneration cleaning. Use single or multi-chamber electrolytic cell processors to electrolyze water, and use water pumps to realize water circulation between processors and activated carbon containers. The higher the current density, the higher the processing efficiency, and the current density range is between 100-5000Am -2 .

本发明利用电化学方法清洗有机物的工作原理是:金刚石膜电极作阳极在电解水时,由于金刚石膜电极的析氧电位很高,金刚石的电极电势(>+3V),在氧气未析出时,就能在电极表面S能产生大量的氢氧自由基(OH·):The working principle of the present invention utilizing the electrochemical method to clean organic matter is: when the diamond film electrode is used as the anode to electrolyze water, since the oxygen evolution potential of the diamond film electrode is very high, the electrode potential (>+3V) of the diamond will not be released when oxygen is released. A large number of hydroxyl radicals (OH ) can be generated on the electrode surface S:

S在阳极表面,S(HO·)是电极表面的氢氧自由基(OH·)。在一般的反应的电极上,吸附了的HO·会使电极钝化,但是在比较稳定的电极上,比如说金刚石膜电极,会把吸附的S(HO·)通过氧化生成氧气:S is on the surface of the anode, and S(HO·) is the hydroxyl radical (OH·) on the electrode surface. On a general reaction electrode, the adsorbed HO will passivate the electrode, but on a relatively stable electrode, such as a diamond film electrode, the adsorbed S(HO ) will be oxidized to generate oxygen:

氧气可以进一步被电极表面的氢氧自由基氧化成O3,Oxygen can be further oxidized to O3 by hydroxyl radicals on the electrode surface,

除了O3外,S(HO.)通过在结合生成H202 In addition to O 3 , S(HO.) generates H 2 0 2 by combining

羟基自由基以及臭氧等粒子具有很高的氧化性,这对于有效的光刻胶剥离和有机清洗非常重要。羟基自由基是有机清洗的关键。活性炭再生是将吸附在活性炭表面的有机废物清除,氧自由基(O·)、臭氧(O3)、过氧化氢(H2O2)以及羟自由基(OH·)等高强度氧化试剂可以实现对这些有机物的氧化清除,从而实现活性炭的再生。Hydroxyl radicals, as well as particles such as ozone, are highly oxidizing, which is important for effective photoresist stripping and organic cleaning. Hydroxyl radicals are the key to organic cleaning. Activated carbon regeneration is to remove organic waste adsorbed on the surface of activated carbon. High-strength oxidizing agents such as oxygen radicals (O·), ozone (O 3 ), hydrogen peroxide (H 2 O 2 ) and hydroxyl radicals (OH·) can Realize the oxidation and removal of these organic substances, so as to realize the regeneration of activated carbon.

实施例一:将高温石蜡均匀涂在抛光硅片上,厚度为1mm,然后将其放入单电极组单厢电解池处理装置中,相邻阴阳电极间距为1mm,电压为10V,电流为2.5A,电流密度在1000Am-2左右。处理1个小时后,石蜡有明显的脱落现象,2小时后石蜡全部脱落,无残留。Example 1: Apply high-temperature paraffin evenly on a polished silicon wafer with a thickness of 1mm, and then put it into a single-electrode group single-compartment electrolytic cell processing device, the distance between adjacent negative and positive electrodes is 1mm, the voltage is 10V, and the current is 2.5 A, the current density is around 1000Am -2 . After 1 hour of treatment, the paraffin wax has obvious shedding phenomenon, and after 2 hours, the paraffin wax all falls off without residue.

实施例二:将高温石蜡均匀涂在抛光硅片上,厚度为1mm,然后将其放入单电极组双厢电解池处理装置阳极槽中,相邻阴阳电极间距为2mm,电压为13V,电流2.5A,电流密度在1000Am-2左右。处理0.5小时后,石蜡有明显的脱落现象,70分钟后石蜡全部脱落,无残留。Example 2: Apply high-temperature paraffin evenly on a polished silicon wafer with a thickness of 1mm, and then put it into the anode tank of the single-electrode group double-chamber electrolytic cell processing device, the distance between adjacent cathode and anode electrodes is 2mm, the voltage is 13V, and the current 2.5A, the current density is around 1000Am -2 . After 0.5 hours of treatment, the paraffin wax has obvious shedding phenomenon, and after 70 minutes, the paraffin wax all falls off without residue.

实施例三:将高温石蜡均匀涂在抛光硅片上,厚度为1mm,然后将其放入多电极组单厢电解池处理装置中,相邻阴阳电极间距为1mm,电压为10V,电流100A,电流密度在7000Am-2左右。处理2min后,石蜡有明显的脱落现象,10min后石蜡全部脱落,无残留。Embodiment 3: Apply high-temperature paraffin evenly on the polished silicon wafer with a thickness of 1 mm, and then put it into a multi-electrode group single-compartment electrolytic cell processing device, the distance between adjacent negative and positive electrodes is 1 mm, the voltage is 10 V, and the current is 100 A. The current density is around 7000Am -2 . After 2 minutes of treatment, the paraffin wax obviously fell off, and after 10 minutes, the paraffin wax completely fell off without residue.

实施例四:将饱和的活性炭置入容器中,将单厢多电极组电化学氧化处理器与容器连接,相邻阴阳电极间距为0.5mm,用水泵实现水在装置与容器之间的循环。通入直流电,电压为10V,电流为5A,电流密度在1000Am-2左右。经过5小时的清洗后,将活性炭从容器中取出,经测试可知活性炭的活性恢复为初始状态。Embodiment 4: Put saturated activated carbon into the container, connect the single-compartment multi-electrode group electrochemical oxidation processor to the container, the distance between adjacent cathode and anode electrodes is 0.5mm, and use a pump to realize water circulation between the device and the container. Connect direct current, the voltage is 10V, the current is 5A, and the current density is around 1000Am -2 . After 5 hours of cleaning, the activated carbon was taken out from the container, and it was tested that the activity of the activated carbon returned to its original state.

Claims (8)

1. A method for cleaning organic matter by an electrochemical method is characterized in that a cleaning object containing the organic matter is placed in an electrolyte; using diamond film electrode as anode, at current density of 100-5000Am-2In the range between electrochemical Oxidation of Hydroxyl (OH) groups in water-) Generating hydroxyl free radical (OH) and oxygen free radical (O), ozone (O)3) And hydrogen peroxide (H)2O2)。
2. An electrochemical cleaning apparatus for use in a method of electrochemically cleaning organic matter according to claim 1, comprising an electrolytic cell, electrodes, and an ionic membrane, wherein said electrolytic cell is a single-compartment electrolytic cell or a two-compartment or multi-compartment electrolytic cell, and the electrolytic cells of the two-compartment and multi-compartment electrolytic cells are separated by the ionic membrane; the electrodes are one or more groups, each group of electrode group consists of an anode-diamond membrane electrode and a cathode-common metal electrode, and the distance between two adjacent electrodes of the anode and the cathode is 0.5-50 mm; and meanwhile, the disturbance of the electrolyte is realized by a mechanicalmode.
3. An electrochemical cleaning device according to claim 4, wherein the electrolyte in said electrolytic cell is connected to a container for objects to be cleaned through a circulation line and a circulation pump.
4. An electrochemical cleaning device according to claim 4 or 5, wherein said electrolytic cell is a two-compartment or multi-compartment electrolytic cell and the circulation line is in communication with the anode tank.
5. An electrochemical cleaning device according to claim 4 or 5, wherein said plurality of electrode sets are connected in parallel or in series.
6. An electrochemical cleaning device according to claim 6, wherein said plurality of electrode sets are connected in parallel or in series.
7. An electrochemical cleaning device according to claim 4 or 5 or 8, wherein said disturbance of the electrolyte is achieved mechanically by means of a pump or agitator.
8. An electrochemical cleaning device according to claim 7, wherein said disturbance of the electrolyte by mechanical means is a water pump or agitator.
CN 200610013851 2006-05-25 2006-05-25 Method and device for cleaning organic matter using electrochemical method Pending CN1884631A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200610013851 CN1884631A (en) 2006-05-25 2006-05-25 Method and device for cleaning organic matter using electrochemical method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200610013851 CN1884631A (en) 2006-05-25 2006-05-25 Method and device for cleaning organic matter using electrochemical method

Publications (1)

Publication Number Publication Date
CN1884631A true CN1884631A (en) 2006-12-27

Family

ID=37582934

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200610013851 Pending CN1884631A (en) 2006-05-25 2006-05-25 Method and device for cleaning organic matter using electrochemical method

Country Status (1)

Country Link
CN (1) CN1884631A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102021639A (en) * 2010-11-10 2011-04-20 安徽华东光电技术研究所 Electrolytic degreasing process for traveling wave tube parts
CN102614537A (en) * 2012-04-19 2012-08-01 牡丹江师范学院 Air purification method and air purification device using same
CN101662961B (en) * 2007-05-10 2013-09-11 仓敷纺织株式会社 Method of washing and apparatus for use therein
CN103727599A (en) * 2014-01-08 2014-04-16 波鹰(厦门)科技有限公司 Air cleaning device and method for removing formaldehyde and PM2.5
CN108404678A (en) * 2018-03-23 2018-08-17 中海油天津化工研究设计院有限公司 A kind of MBR films off-line cleaning device and cleaning method
CN113600549A (en) * 2021-09-10 2021-11-05 何龙 Method for electrochemically degrading organic pollutants outside cell and application

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101662961B (en) * 2007-05-10 2013-09-11 仓敷纺织株式会社 Method of washing and apparatus for use therein
CN102021639A (en) * 2010-11-10 2011-04-20 安徽华东光电技术研究所 Electrolytic degreasing process for traveling wave tube parts
CN102614537A (en) * 2012-04-19 2012-08-01 牡丹江师范学院 Air purification method and air purification device using same
CN102614537B (en) * 2012-04-19 2014-07-23 牡丹江师范学院 Air purification method and air purification device using same
CN103727599A (en) * 2014-01-08 2014-04-16 波鹰(厦门)科技有限公司 Air cleaning device and method for removing formaldehyde and PM2.5
CN108404678A (en) * 2018-03-23 2018-08-17 中海油天津化工研究设计院有限公司 A kind of MBR films off-line cleaning device and cleaning method
CN113600549A (en) * 2021-09-10 2021-11-05 何龙 Method for electrochemically degrading organic pollutants outside cell and application
CN113600549B (en) * 2021-09-10 2023-08-22 何龙 Method for electrochemical degradation of organic pollutants outside tank and application

Similar Documents

Publication Publication Date Title
Jin et al. Micro-electrolysis technology for industrial wastewater treatment
CN108529714B (en) Photoelectrochemical reaction cell and method for treating hydrogen sulfide waste gas and wastewater
US8313657B1 (en) Method and system for removal of ammonia from wastewater by electrolysis
CN1884631A (en) Method and device for cleaning organic matter using electrochemical method
CN111517428B (en) Treatment process and system for removing heavy metal ions in PTA wastewater
CN108358363A (en) A kind of deep treatment method of organic sewage with high salt
CN109095698A (en) One kind filtering industrial waste water high-efficiency processing equipment based on electrochemistry and film
CN106745532A (en) A kind of processing method of antibiotic waste water
CN101618905A (en) Method for treating phosphoric wastewater through ozone-enhanced electrocoagulation
CN208182760U (en) A kind of heavy metal wastewater treatment apparatus
CN201317696Y (en) Persistent organic waste water electrolytic oxidation device
CN204162479U (en) A New Electrochemical Treatment Equipment for Wastewater Treatment
CN105692801B (en) Utilize the method for estriol in 3 D electrode reactor treated sewage
CN105198049A (en) Method of sewage treatment
CN210215032U (en) Electrode plate effluent treatment plant
CN105016537A (en) Plug flow type dual-electrode electrolysis air floater
CN116282470A (en) Advanced treatment method for organic pollutants in landfill leachate
CN112374666B (en) Three-dimensional electrolytic sewage treatment method
CN212050667U (en) Waste water treatment device
KR101560245B1 (en) Treatment apparatus for waste washing water of wet scrubber
CN207671827U (en) A kind of electroplating sewerage processing equipment
CN209619059U (en) A kind of system handling high toxicity high-COD waste water
CN214167702U (en) Advanced treatment system for refining wastewater
CN212669432U (en) Device for treating sulfur-containing wastewater of oil and gas field
CN110818038A (en) Method for treating titanium or titanium alloy pickling waste liquid by capacitive deionization technology

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication