[go: up one dir, main page]

CN1323950C - Pulse plasma gas-liquid discharge equipment for waste water treatment - Google Patents

Pulse plasma gas-liquid discharge equipment for waste water treatment Download PDF

Info

Publication number
CN1323950C
CN1323950C CNB200510049452XA CN200510049452A CN1323950C CN 1323950 C CN1323950 C CN 1323950C CN B200510049452X A CNB200510049452X A CN B200510049452XA CN 200510049452 A CN200510049452 A CN 200510049452A CN 1323950 C CN1323950 C CN 1323950C
Authority
CN
China
Prior art keywords
needle
electrode
horizontal partition
cylinder
horizontal
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
CNB200510049452XA
Other languages
Chinese (zh)
Other versions
CN1673102A (en
Inventor
雷乐成
周明华
郝小龙
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.)
Zhejiang University ZJU
Original Assignee
Zhejiang University ZJU
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 Zhejiang University ZJU filed Critical Zhejiang University ZJU
Priority to CNB200510049452XA priority Critical patent/CN1323950C/en
Publication of CN1673102A publication Critical patent/CN1673102A/en
Application granted granted Critical
Publication of CN1323950C publication Critical patent/CN1323950C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

本发明涉及用于废水处理的脉冲等离子体气液放电装置包括具有水平隔板的绝缘筒,水平隔板与筒体下部形成曝气室,在绝缘筒的盖板上拧有金属螺杆,金属螺杆伸入筒端固定有水平板式电极,水平隔板上均布有曝气孔,曝气孔中置有针状电极,针状电极或有轴向通孔或与曝气孔间有间隙,针状电极的针尖露于水平隔板的上方,并与板式电极平行,针状电极和板式电极与脉冲电源输出端相连。处理废水时,曝气室向绝缘筒内的废水曝气,电极放电产生的气相活性粒子,促使气相活性粒子向液相扩散,并与液相产生的活性粒子协同降解有机污染物。该装置结构简单,操作简便,运行成本低。可用于处理难生物降解及有毒有害工业废水和病毒微生物去除净化。

Figure 200510049452

The invention relates to a pulse plasma gas-liquid discharge device for wastewater treatment, which comprises an insulating cylinder with a horizontal partition, the horizontal partition and the lower part of the cylinder form an aeration chamber, and a metal screw is screwed on the cover plate of the insulating cylinder, and the metal screw is A horizontal plate electrode is fixed at the end of the barrel, and aeration holes are evenly distributed on the horizontal partition. There are needle-shaped electrodes in the aeration holes. The needle-shaped electrodes either have axial through holes or have gaps with the aeration holes. The needle tip of the electrode is exposed above the horizontal partition and is parallel to the plate electrode, and the needle electrode and the plate electrode are connected to the output end of the pulse power supply. When treating wastewater, the aeration chamber aerates the wastewater in the insulating cylinder, and the gas-phase active particles generated by electrode discharge promote the diffusion of gas-phase active particles to the liquid phase, and cooperate with the active particles generated in the liquid phase to degrade organic pollutants. The device has the advantages of simple structure, convenient operation and low operation cost. It can be used for the treatment of refractory biodegradable and toxic and harmful industrial wastewater and the removal and purification of viruses and microorganisms.

Figure 200510049452

Description

用于废水处理的脉冲等离子体气液放电装置Pulse plasma gas-liquid discharge device for wastewater treatment

技术领域technical field

本发明涉及一种利用脉冲电源在气液两相中放电处理废水的装置,属于环境技术和水处理领域。The invention relates to a device for discharging waste water in gas-liquid two-phase by using a pulse power supply, which belongs to the field of environmental technology and water treatment.

背景技术Background technique

针对目前工业生产中所排放的大量工业废水,其种类繁多,成分复杂,化学需氧量(COD)浓度高,可生化性差,有毒有害等特点,采用常规物化或生化处理技术已很难有效地控制与治理。因此,高级氧化技术成为当今处理难生物降解及有毒有害工业废水的新技术和新方法。In view of the large amount of industrial wastewater discharged in the current industrial production, it has various types, complex components, high concentration of chemical oxygen demand (COD), poor biodegradability, toxic and harmful characteristics, and it is difficult to effectively treat it with conventional physicochemical or biochemical treatment technologies. Control and Governance. Therefore, advanced oxidation technology has become a new technology and new method for the treatment of refractory biodegradable and toxic and harmful industrial wastewater.

高级氧化技术利用各种活性自由基攻击工业废水中的大分子有机物(或微生物),破坏其分子结构(或细胞),从而使有机废水得以净化。但是,由于高级氧化技术存在反应条件苛刻、选择性差、成本高等缺点,致使其在进一步推广上具有一定的局限性和适应范围。最近,一种新型的高级氧化技术,液相电脉冲技术由于高压脉冲放电在电子传输过程能量释放的多样性和其在环境污染治理方面的应用引起了广泛的关注。Advanced oxidation technology uses various active free radicals to attack macromolecular organic matter (or microorganisms) in industrial wastewater, destroying its molecular structure (or cells), so that organic wastewater can be purified. However, due to the disadvantages of harsh reaction conditions, poor selectivity, and high cost, the advanced oxidation technology has certain limitations and scope of application in its further promotion. Recently, a new type of advanced oxidation technology, liquid-phase electric pulse technology, has attracted widespread attention due to the diversity of energy release in the electron transfer process of high-voltage pulse discharge and its application in environmental pollution control.

液电脉冲技术一般采用高压脉冲电源形成等离子体,它集合高能电子辐射、湿式氧化、化学氧化、光催化氧化等高级氧化技术于一体,系统不需要外加氧化剂,反应体系无需辅以高温、高压或外加光源等技术手段,是一种全新概念的废水处理新技术。水中高压脉冲放电电压上升时间短(<100ns),脉冲宽度窄(<200ns),因而可以在不使电场内的离子加速的情况下,单使电子加速,从而形成无需屏蔽的高能自由电子,这些高能自由电子将促使有机物的激发裂解或电离。这一过程同时具有物理效应和化学效应,物理效应可形成紫外光和冲击波,其强度取决于放电的能量;化学效应主要促使活性物质的形成,如:OH·、O·、H2O2、O3等各种活性自由基,因而高压脉冲放电处理废水可利用放电形成的紫外光、冲击波以及活性自由基,形成高能电子、紫外线、臭氧等多因素的协同降解作用,增强处理效果,是集光、电、化学氧化于一体的新型水处理技术Hydroelectric pulse technology generally uses high-voltage pulse power to form plasma, which integrates advanced oxidation technologies such as high-energy electron radiation, wet oxidation, chemical oxidation, and photocatalytic oxidation. Adding technical means such as light source is a new concept of new wastewater treatment technology. The rising time of the high-voltage pulse discharge voltage in water is short (<100ns), and the pulse width is narrow (<200ns), so it can accelerate the electrons without accelerating the ions in the electric field, thereby forming high-energy free electrons without shielding. High-energy free electrons will promote the excited cracking or ionization of organic matter. This process has both physical and chemical effects. Physical effects can form ultraviolet light and shock waves, and their strength depends on the energy of the discharge; chemical effects mainly promote the formation of active substances, such as: OH·, O·, H 2 O 2 , O 3 and other active free radicals, so the high-voltage pulse discharge treatment of wastewater can use the ultraviolet light, shock waves and active free radicals formed by the discharge to form a synergistic degradation of high-energy electrons, ultraviolet rays, ozone and other factors to enhance the treatment effect. New water treatment technology integrating light, electricity and chemical oxidation

气相高压脉冲放电也是通过气相高压放电产生等离子体,从而激发生成活性粒子,去除有机有害恶臭废气,已广范应用于工业有机废气处理工艺中。目前,常用的高压放电等离子体方法水处理反应器的电极结构主要有液面下点(针)—板、线—板、线—筒结构形式,但有混合不均,产生死角,活性自由基产率不高,扩散迁移速率较低等缺点。Gas-phase high-voltage pulse discharge also generates plasma through gas-phase high-voltage discharge, thereby stimulating the generation of active particles and removing organic harmful and odorous waste gas. It has been widely used in industrial organic waste gas treatment processes. At present, the electrode structure of the commonly used high-voltage discharge plasma method water treatment reactor mainly includes point (needle)-plate, line-plate, line-cylinder structures under the liquid surface, but there are uneven mixing, dead angles, and active free radicals. The yield is not high, and the diffusion migration rate is low.

发明内容Contents of the invention

本发明的目的是提供一种采用液下针尖曝气处理废水的脉冲等离子体气液放电装置,利用针尖曝气在高压脉冲气液两相放电的条件下,产生更多的活性粒子,增强活性物质向液相传质扩散,实现更高效的水体杀菌,提高有机污染物的去除效益。The purpose of the present invention is to provide a pulse plasma gas-liquid discharge device that uses submerged needle-point aeration to treat wastewater, using needle-point aeration to generate more active particles and enhance the activity under the condition of high-voltage pulse gas-liquid two-phase discharge Substances diffuse to the liquid phase mass transfer to achieve more efficient water sterilization and improve the removal efficiency of organic pollutants.

为达上述目的,本发明有以下两种技术解决方案。To achieve the above object, the present invention has the following two technical solutions.

方案1plan 1

用于废水处理的脉冲等离子体气液放电装置,包括具有水平隔板的绝缘筒,水平隔板与筒体下部形成曝气室,在绝缘筒的盖板上拧有金属螺杆,金属螺杆的一端伸入筒中,该端固定有水平板式电极,在水平隔板上均布有曝气孔,固定在绝缘筒筒底的针状电极穿越曝气孔并与曝气孔间留有间隙,针状电极的针尖处于与水平板式电极平行的同一平面,在水平隔板上方的筒壁设有进水口和出水口,水平隔板下方的筒壁设有进气孔,针状电极和板式电极分别与脉冲电源的两个输出端相连。Pulse plasma gas-liquid discharge device for wastewater treatment, including an insulating cylinder with a horizontal partition, the horizontal partition and the lower part of the cylinder form an aeration chamber, a metal screw is screwed on the cover plate of the insulating cylinder, and one end of the metal screw Extending into the cylinder, the end is fixed with a horizontal plate electrode, and there are aeration holes evenly distributed on the horizontal partition. The needle tip of the electrode is in the same plane parallel to the horizontal plate electrode. The cylinder wall above the horizontal partition is provided with water inlet and outlet, and the cylinder wall below the horizontal partition is provided with an air inlet. The needle electrode and the plate electrode are respectively connected to the The two output terminals of the pulse power supply are connected.

方案2Scenario 2

用于废水处理的脉冲等离子体气液放电装置,包括具有水平隔板的绝缘筒,水平隔板与筒体下部形成曝气室,在绝缘筒的盖板上拧有金属螺杆,金属螺杆的一端伸入筒中,该端固定有水平板式电极,在水平隔板上均布固定有垂直于隔板的针状电极,针状电极的针尖处于与水平板式电极平行的同一平面,针状电极具有与曝气室相通的轴向通孔,在水平隔板上方的筒壁设有进水口和出水口,水平隔板下方的筒壁设有进气孔,针状电极和板式电极分别与脉冲电源的两个输出端相连。Pulse plasma gas-liquid discharge device for wastewater treatment, including an insulating cylinder with a horizontal partition, the horizontal partition and the lower part of the cylinder form an aeration chamber, a metal screw is screwed on the cover plate of the insulating cylinder, and one end of the metal screw Extending into the barrel, the end is fixed with a horizontal plate electrode, and evenly distributed on the horizontal separator, needle electrodes perpendicular to the separator are fixed. The needle tip of the needle electrode is in the same plane parallel to the horizontal plate electrode, and the needle electrode has Axial through holes connected to the aeration chamber, water inlet and outlet are provided on the cylinder wall above the horizontal partition, air inlet holes are provided on the cylinder wall below the horizontal partition, the needle electrode and the plate electrode are connected with the pulse power supply respectively. The two outputs are connected.

处理废水时,曝气室通过针状电极的轴向通孔或者通过针状电极与曝气孔的间隙向绝缘筒内的废水曝入空气,脉冲电源通过电极进行放电,气体通过针尖放电时产生气液混合放电形式,使气相放电产生的活性物质迅速地扩散传质到水体中,并与液下曝气水体产生强烈混合,提高活性物质产率,更大程度上提高了处理效率,同时通过螺杆调节板式电极与针状电极的间距,可实现在液面上或液面下的放电方式,出现不同的放电形式,如电晕放电、流柱放电和火花放电形式。通过在水平隔板均布相当数量的针状电极实现均匀分布曝气,能有效地提高气液传质混合,提高处理废水的效率。When treating wastewater, the aeration chamber exposes air to the wastewater in the insulating cylinder through the axial through hole of the needle electrode or through the gap between the needle electrode and the aeration hole. The gas-liquid mixed discharge form enables the active substances generated by gas-phase discharge to rapidly diffuse and transfer to the water body, and strongly mix with the submerged aerated water body to increase the yield of active substances and improve the treatment efficiency to a greater extent. At the same time, through The screw adjusts the distance between the plate electrode and the needle electrode, which can realize the discharge mode on the liquid surface or below the liquid surface, and there are different discharge forms, such as corona discharge, streamer discharge and spark discharge. Evenly distributed aeration is realized by uniformly distributing a considerable number of needle-shaped electrodes on the horizontal partition, which can effectively improve gas-liquid mass transfer and mixing, and improve the efficiency of wastewater treatment.

本发明装置结构简单,操作简便,利用无价值的空气可以产生更多活性物质,运行成本低。本发明装置在气液两相混合放电环境下,提高了放电强度,从而大大提高了水体中的活性物质的产生效率,增强水处理效果。增强气相活性物质向液相传质扩散,起到了气液混合放电的协同效应。本发明装置可用于处理难生物降解及有毒有害工业废水和病毒微生物去除净化。The device of the invention is simple in structure and easy to operate, can generate more active substances by utilizing useless air, and has low operating cost. The device of the invention improves the discharge intensity in a gas-liquid two-phase mixed discharge environment, thereby greatly improving the production efficiency of active substances in the water body and enhancing the water treatment effect. Enhancing the mass transfer and diffusion of gas-phase active substances to liquid phase plays a synergistic effect of gas-liquid mixed discharge. The device of the invention can be used for treating refractory biodegradable and toxic and harmful industrial waste water and removing and purifying viruses and microorganisms.

附图说明Description of drawings

图1是方案1的脉冲等离子体气液放电水处理装置结构示意图;Fig. 1 is the structural representation of the pulse plasma gas-liquid discharge water treatment device of scheme 1;

图2是方案2的脉冲等离子体气液放电水处理装置结构示意图。Fig. 2 is a schematic structural diagram of the pulse plasma gas-liquid discharge water treatment device of Scheme 2.

具体实施方式Detailed ways

参照图1,用于废水处理的脉冲等离子体气液放电装置,包括具有水平隔板14的绝缘筒10,绝缘筒可以是绝缘有机玻璃圆筒,水平隔板14与筒体下部形成曝气室12,在绝缘筒的盖板11上拧有金属螺杆3,金属螺杆3的一端伸入筒中,该端固定有水平板式电极4,板式电极可以采用不锈钢圆板,在水平隔板14上均布有曝气孔13,通常使均布区域与板式电极4相对应,与曝气孔相应数量的实心针状电极9穿越曝气孔13固定在绝缘筒10的筒底,针状电极9与曝气孔13间留有间隙,针状电极9的针尖露于水平隔板14的上方,并处于同一平面,与水平板式电极4平行,在水平隔板14上方的筒壁设有进水口6和出水口7,水平隔板14下方的筒壁设有进气孔8,针状电极9和板式电极4分别与脉冲电源1的两个输出端相连,图中2为接地线,5为连接导线。Referring to Fig. 1, the pulse plasma gas-liquid discharge device for wastewater treatment includes an insulating cylinder 10 with a horizontal partition 14, the insulating cylinder can be an insulating plexiglass cylinder, and the horizontal partition 14 and the lower part of the cylinder form an aeration chamber 12. A metal screw 3 is screwed on the cover plate 11 of the insulating cylinder. One end of the metal screw 3 extends into the cylinder. The end is fixed with a horizontal plate electrode 4. The plate electrode can be a stainless steel circular plate, which is evenly distributed on the horizontal separator 14. There are aeration holes 13, usually the evenly distributed area corresponds to the plate electrode 4, and the solid needle electrodes 9 corresponding to the number of aeration holes pass through the aeration holes 13 and are fixed on the bottom of the insulating cylinder 10, and the needle electrodes 9 are connected to the aeration holes. There is a gap between the air holes 13, and the needle point of the needle electrode 9 is exposed above the horizontal partition 14, and is on the same plane, parallel to the horizontal plate electrode 4, and the cylinder wall above the horizontal partition 14 is provided with a water inlet 6 and The water outlet 7, the cylinder wall below the horizontal partition 14 are provided with an air inlet 8, the needle electrode 9 and the plate electrode 4 are respectively connected to the two output ends of the pulse power supply 1, 2 in the figure is the ground wire, and 5 is the connecting wire .

参照图2,用于废水处理的脉冲等离子体气液放电装置,包括具有水平隔板14的绝缘筒10,水平隔板14与筒体下部形成曝气室12,在绝缘筒的盖板11上拧有金属螺杆3,金属螺杆3的一端伸入筒中,该端固定有水平板式电极4,在水平隔板14上均布固定有垂直于隔板14的针状电极9,通常使针状电极9均布区域与板式电极4相对应,针状电极9的针尖处于同一平面,并与水平板式电极4平行,针状电极9具有与曝气室12相通的轴向通孔15,在水平隔板14上方的筒壁设有进水口6和出水口7,水平隔板14下方的筒壁设有进气孔8,针状电极9和板式电极4分别与脉冲电源1的两个输出端相连,图中2为接地线,5为连接导线。Referring to Fig. 2, the pulse plasma gas-liquid discharge device for wastewater treatment includes an insulating cylinder 10 with a horizontal partition 14, the horizontal partition 14 and the lower part of the cylinder form an aeration chamber 12, and on the cover plate 11 of the insulating cylinder A metal screw 3 is screwed, and one end of the metal screw 3 extends into the barrel, and the end is fixed with a horizontal plate electrode 4, and the needle-shaped electrodes 9 perpendicular to the separator 14 are evenly distributed on the horizontal separator 14, and the needle-shaped electrodes are usually 9. The evenly distributed area corresponds to the plate electrode 4. The needle tip of the needle electrode 9 is in the same plane and parallel to the horizontal plate electrode 4. The needle electrode 9 has an axial through hole 15 communicating with the aeration chamber 12. The cylinder wall above the plate 14 is provided with a water inlet 6 and a water outlet 7, and the cylinder wall below the horizontal partition 14 is provided with an air inlet 8, and the needle electrode 9 and the plate electrode 4 are respectively connected to the two output ends of the pulse power supply 1 , 2 in the figure is the ground wire, and 5 is the connecting wire.

上述两种方案中所说的脉冲电源为4-37型高功率重复频率脉冲电源,电源参数为:峰值电压1-50KV,脉冲上升前沿80-200ns,脉冲重复频率20-250Hz。The pulse power supply mentioned in the above two schemes is a 4-37 type high-power repetition frequency pulse power supply. The power supply parameters are: peak voltage 1-50KV, pulse rising edge 80-200ns, pulse repetition frequency 20-250Hz.

以下为采用本发明装置处理废水的试验比较,以对氯苯酚、邻氯苯酚、甲基红和阳离子红X-GRL为污染物,电源参数:电压峰值(19.6KV),脉冲前沿(100ns左右),脉冲频率:(150Hz),在液下电极间距为2mm(针状电极和板式电极均在水下),液上电极间距为4mm(针状电极在水下,板式电极在水上),板式电极与液面距离为1mm,在此条件下,去除效率可达95%以上,电源总能耗小于20W,分别比同条件下无曝气方式的处理效果好20%左右,达到同样去除率时,所需的处理时间短10min,能耗减少25%左右。实验条件和测试数据及结果如表1所示。The following is the test comparison of adopting the device of the present invention to treat waste water, with p-chlorophenol, o-chlorophenol, methyl red and cationic red X-GRL as pollutants, power supply parameters: peak voltage (19.6KV), pulse front (about 100ns) , pulse frequency: (150Hz), the electrode spacing under the liquid is 2mm (needle electrodes and plate electrodes are both underwater), the electrode spacing above the liquid is 4mm (needle electrodes are under water, plate electrodes are above water), plate electrodes The distance from the liquid surface is 1mm. Under this condition, the removal efficiency can reach more than 95%, and the total energy consumption of the power supply is less than 20W, which is about 20% better than the treatment effect without aeration under the same conditions. When the same removal rate is reached, The required processing time is 10 minutes shorter, and the energy consumption is reduced by about 25%. The experimental conditions, test data and results are shown in Table 1.

表1 污染物   放电方式   曝气量(空气)(L/h)   初始浓度(mg/L)   时间(min)   最终浓度(mg/L)   去除率(%)   电源能耗(W) 对氯苯酚   液下   0100   100100   3030   36.12.5   63.997.58   18.512.6 液上   060   100100   3030   32.13.5   67.996.5   19.310.8 邻氯苯酚   液下   0100   100100   3030   25.71.2   74.398.8   17.59.6 液上   0100   100100   3030   23.82.1   76.297.8   20.68.6 甲基红   液下   060   5050   3030   12.32.3   75.495.4   16.58.7   液上   060   5050   3030   13.62.9   72.894.2   15.47.2 阳离子红X-GRL 液下   015   5050   6060   12.11.3   75.897.4   17.312.1 液上   015   5050   6060   11.61.0   76.898.0   18.112.6 Table 1 Pollutants discharge method Aeration volume (air) (L/h) Initial concentration (mg/L) time (min) Final concentration (mg/L) Removal rate (%) Power Consumption(W) p-Chlorophenol underwater 0100 100100 3030 36.12.5 63.997.58 18.512.6 liquid on 060 100100 3030 32.13.5 67.996.5 19.310.8 o-Chlorophenol underwater 0100 100100 3030 25.71.2 74.398.8 17.59.6 liquid on 0100 100100 3030 23.82.1 76.297.8 20.68.6 Methyl red underwater 060 5050 3030 12.32.3 75.495.4 16.58.7 liquid on 060 5050 3030 13.62.9 72.894.2 15.47.2 Cationic Red X-GRL underwater 015 5050 6060 12.11.3 75.897.4 17.312.1 liquid on 015 5050 6060 11.61.0 76.898.0 18.112.6

Claims (2)

1.用于废水处理的脉冲等离子体气液放电装置,其特征是包括具有水平隔板(14)的绝缘筒(10),水平隔板(14)与筒体下部形成曝气室(12),在绝缘筒的盖板(11)上拧有金属螺杆(3),金属螺杆(3)的一端伸入筒中,该端固定有水平板式电极(4),在水平隔板(14)上均布有曝气孔(13),固定在绝缘筒(10)筒底的针状电极(9)穿越曝气孔(13)并与曝气孔(13)间留有间隙,针状电极(9)的针尖处于与水平板式电极(4)平行的同一平面,在水平隔板(14)上方的筒壁设有进水口(6)和出水口(7),水平隔板(14)下方的筒壁设有进气孔(8),针状电极(9)和板式电极(4)分别与脉冲电源(1)的两个输出端相连。1. The pulse plasma gas-liquid discharge device for wastewater treatment is characterized in that it comprises an insulating cylinder (10) with a horizontal partition (14), and the horizontal partition (14) and the lower part of the cylinder form an aeration chamber (12) , a metal screw (3) is screwed on the cover plate (11) of the insulating cylinder, and one end of the metal screw (3) extends into the cylinder, and this end is fixed with a horizontal plate electrode (4), which is evenly spaced on the horizontal separator (14). Aeration holes (13) are arranged on the cloth, and needle-shaped electrodes (9) fixed on the bottom of the insulating cylinder (10) pass through the aeration holes (13) and leave a gap with the aeration holes (13). The needle-shaped electrodes (9) ) in the same plane parallel to the horizontal plate electrode (4), the cylinder wall above the horizontal partition (14) is provided with a water inlet (6) and a water outlet (7), and the cylinder below the horizontal partition (14) The wall is provided with an air inlet (8), and the needle electrode (9) and the plate electrode (4) are respectively connected with two output terminals of the pulse power supply (1). 2.用于废水处理的脉冲等离子体气液放电装置,其特征是包括具有水平隔板(14)的绝缘筒(10),水平隔板(14)与筒体下部形成曝气室(12),在绝缘筒的盖板(11)上拧有金属螺杆(3),金属螺杆(3)的一端伸入筒中,该端固定有水平板式电极(4),在水平隔板(14)上均布固定有垂直于隔板(14)的针状电极(9),针状电极(9)的针尖处于与水平板式电极(4)平行的同一平面,针状电极(9)具有与曝气室(12)相通的轴向通孔(15),在水平隔板(14)上方的筒壁设有进水口(6)和出水口(7),水平隔板(14)下方的筒壁设有进气孔(8),针状电极(9)和板式电极(4)分别与脉冲电源(1)的两个输出端相连。2. The pulse plasma gas-liquid discharge device for wastewater treatment is characterized in that it includes an insulating cylinder (10) with a horizontal partition (14), and the horizontal partition (14) and the lower part of the cylinder form an aeration chamber (12) , a metal screw (3) is screwed on the cover plate (11) of the insulating cylinder, and one end of the metal screw (3) extends into the cylinder, and this end is fixed with a horizontal plate electrode (4), which is evenly spaced on the horizontal separator (14). The needle electrode (9) perpendicular to the separator (14) is fixed on the cloth, the needle point of the needle electrode (9) is in the same plane parallel to the horizontal plate electrode (4), and the needle electrode (9) has a (12) Connected axial through holes (15), the cylinder wall above the horizontal partition (14) is provided with water inlet (6) and water outlet (7), and the cylinder wall below the horizontal partition (14) is provided with The air inlet (8), the needle electrode (9) and the plate electrode (4) are respectively connected with two output terminals of the pulse power supply (1).
CNB200510049452XA 2005-03-24 2005-03-24 Pulse plasma gas-liquid discharge equipment for waste water treatment Expired - Fee Related CN1323950C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB200510049452XA CN1323950C (en) 2005-03-24 2005-03-24 Pulse plasma gas-liquid discharge equipment for waste water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB200510049452XA CN1323950C (en) 2005-03-24 2005-03-24 Pulse plasma gas-liquid discharge equipment for waste water treatment

Publications (2)

Publication Number Publication Date
CN1673102A CN1673102A (en) 2005-09-28
CN1323950C true CN1323950C (en) 2007-07-04

Family

ID=35045918

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB200510049452XA Expired - Fee Related CN1323950C (en) 2005-03-24 2005-03-24 Pulse plasma gas-liquid discharge equipment for waste water treatment

Country Status (1)

Country Link
CN (1) CN1323950C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111268763A (en) * 2020-04-01 2020-06-12 浙江阳岭健康科技有限公司 Sterilizer
US12116292B2 (en) 2021-01-14 2024-10-15 Burak Karadag Plasma-based water treatment apparatus

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100371260C (en) * 2006-06-16 2008-02-27 浙江大学 Method of Liquid Phase Plasma Combined with TiO2 Catalytic Treatment of Wastewater
WO2008037065A1 (en) * 2006-09-26 2008-04-03 Chang Qing Xu Method and apparatus of forming domain inversion structures in a nonlinear ferroelectric substrate
CN100446849C (en) * 2006-11-01 2008-12-31 浙江大学 A method and device for synchronously purifying gas and liquid with high-voltage direct current/pulse discharge
CN101254960B (en) * 2008-03-27 2012-12-05 汪峰 Plasma water treatment method and device thereof
CN102838187A (en) * 2011-06-22 2012-12-26 深圳市鑫翔隆环保科技有限公司 Apparatus for water treatment
JP2013022476A (en) * 2011-07-15 2013-02-04 Panasonic Corp Plasma generating apparatus and cleaning/purifying apparatus using the same
BG111044A (en) * 2011-10-03 2013-04-30 Borislav лавБОРИСОВ Борис Borisov Method and a device for receiving plasma
CN103359803B (en) * 2012-04-08 2015-09-30 西北农林科技大学 A kind of water treatment method and device simultaneously removing heavy metal ions in wastewater and organic pollutant
CN103633356B (en) * 2013-12-11 2015-10-28 山东大学 A kind of small-sized microorganism electrolysis cell and application thereof
CN105036251A (en) * 2015-06-26 2015-11-11 南京大学 Device for efficiently degrading high-concentration organic polluted wastewater by corona discharge plasma
CN107364932B (en) * 2017-07-26 2020-03-17 西安交通大学 Device for treating waste liquid based on plasma jet
CN107381723A (en) * 2017-09-04 2017-11-24 南京大学 A kind of sewage-treatment plant using more needle plate gas-liquid discharge in water plasmas
CN112777695A (en) * 2021-01-13 2021-05-11 西安交通大学 Plasma medical waste liquid emergency sterilizing device
CN113548716A (en) * 2021-08-31 2021-10-26 珠海格力电器股份有限公司 A liquid phase discharge reactor
CN115477367B (en) * 2022-09-19 2025-09-23 珠海格力电器股份有限公司 Activated water device and activated water preparation equipment
CN116037010A (en) * 2022-12-21 2023-05-02 浙江工业大学 Gas-liquid reactor
CN117983643A (en) * 2024-03-22 2024-05-07 同济大学 A piston-type dielectric barrier discharge treatment device and its application method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04310503A (en) * 1991-04-03 1992-11-02 Mitsubishi Heavy Ind Ltd Ozonizer
CN1440934A (en) * 2003-04-08 2003-09-10 大连理工大学 Water-treating bipolar pulse discharge process
JP2005058887A (en) * 2003-08-11 2005-03-10 Mitsubishi Heavy Ind Ltd Waste water treatment apparatus using high-voltage pulse

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04310503A (en) * 1991-04-03 1992-11-02 Mitsubishi Heavy Ind Ltd Ozonizer
CN1440934A (en) * 2003-04-08 2003-09-10 大连理工大学 Water-treating bipolar pulse discharge process
JP2005058887A (en) * 2003-08-11 2005-03-10 Mitsubishi Heavy Ind Ltd Waste water treatment apparatus using high-voltage pulse

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111268763A (en) * 2020-04-01 2020-06-12 浙江阳岭健康科技有限公司 Sterilizer
US12116292B2 (en) 2021-01-14 2024-10-15 Burak Karadag Plasma-based water treatment apparatus

Also Published As

Publication number Publication date
CN1673102A (en) 2005-09-28

Similar Documents

Publication Publication Date Title
CN1323950C (en) Pulse plasma gas-liquid discharge equipment for waste water treatment
CN1257846C (en) Bipolar Pulse Discharge Water Treatment Method
CN1229282C (en) Method and device for treating wastewater containing organic matter
CN211570217U (en) Organic waste liquid treatment device of cylinder type DBD plasma
CN102583697B (en) A dielectric barrier discharge water treatment device and its treatment method
CN104211137B (en) Plasma water treatment device
CN100349804C (en) Method for removing difficultly degradable organic substance from packed bed in high voltage pulse electric field
CN103754994B (en) Glow discharge plasma water treatment method and device
CN101759319A (en) Ship ballast water treatment method and discharge reactor
CN110357200A (en) Array gas-liquid discharge device and method for multistage treatment of organic matters in water
CN1454185A (en) Water purification system and method
Cai et al. An evaluation of metronidazole degradation in a plasma-assisted rotating disk reactor coupled with TiO2 in aqueous solution
CN108383207A (en) A kind of oilfield polymer flooding dirt containing PAM water purification method
CN108675388A (en) A kind of purifier and purification method of used water difficult to degradate
CN1663916A (en) High-pressure pulse discharge catalytic oxidation method for removal of undegradable organic substances in water
CN2832800Y (en) Device for photo-catalytic treatment of organic wastewater induced by needle-board type pulse discharge plasma
CN104445528A (en) Device for purifying polluted water by using uniform dielectric barrier discharging plasma
Xiong et al. Removal of formic acid from wastewater using three-phase three-dimensional electrode reactor
CN1316857C (en) Method and device for photo catalytically treating waste water by medium barrier discharging induced semiconductor
CN2780745Y (en) Pulsed plasma gas liquid discharge device for waste water treatment
CN108479341B (en) A device for treating organic flue gas by plasma-assisted iron-carbon micro-electrolysis
CN202508912U (en) Dielectric barrier discharge water treatment device
CN215855561U (en) A processing apparatus for high contain salt organic waste water of difficult degradation
CN113045065B (en) Sliding arc plasma sewage purification system based on spiral electrode structure
CN104310678A (en) Continuous catalytic plasma water pollution purification device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070704

Termination date: 20110324