[go: up one dir, main page]

CN105293644A - Photoelectrochemical electrolytic equipment and electrode plates for photoelectrochemical electrolytic equipment - Google Patents

Photoelectrochemical electrolytic equipment and electrode plates for photoelectrochemical electrolytic equipment Download PDF

Info

Publication number
CN105293644A
CN105293644A CN201510652210.3A CN201510652210A CN105293644A CN 105293644 A CN105293644 A CN 105293644A CN 201510652210 A CN201510652210 A CN 201510652210A CN 105293644 A CN105293644 A CN 105293644A
Authority
CN
China
Prior art keywords
mentioned
coating
electrolyzer
battery lead
sno
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.)
Granted
Application number
CN201510652210.3A
Other languages
Chinese (zh)
Other versions
CN105293644B (en
Inventor
吴允苗
朱君秋
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.)
Quanzhou Normal University
Original Assignee
Quanzhou Normal University
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 Quanzhou Normal University filed Critical Quanzhou Normal University
Priority to CN201510652210.3A priority Critical patent/CN105293644B/en
Publication of CN105293644A publication Critical patent/CN105293644A/en
Application granted granted Critical
Publication of CN105293644B publication Critical patent/CN105293644B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Catalysts (AREA)
  • Physical Water Treatments (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

本发明公开一种光电化学电解设备,包括电解槽及设于电解槽内的石英管、紫外灯和电极板,电极板设置有若干片,呈由上而下间隔排列,电极板的其一半部位表面上涂覆有金属氧化物涂层形成阳极部,另一半部位的表面涂覆有半导体光催化剂涂层形成阴极部,两阴极部之间具有一阳极部,两电极板之间均设置有绝缘间隔件,且各电极板通过绝缘支撑杆串接在一起,石英管竖立穿过各电极板,且石英管的上端端部向上穿出电解槽外。与现有技术相比,其可使紫外光光化学氧化、光催化氧化和电催化氧化处理技术具有协同效应,使污水的整一降解过程迅速,高效,具有结构简易,易维护,拆装方便,制作成本低的优点。本发明还公开一种用于该光电化学电解设备的电极板。

The invention discloses a photoelectrochemical electrolysis device, which comprises an electrolytic cell, a quartz tube, an ultraviolet lamp and an electrode plate arranged in the electrolytic cell. The surface is coated with a metal oxide coating to form the anode part, and the other half of the surface is coated with a semiconductor photocatalyst coating to form the cathode part. There is an anode part between the two cathode parts, and an insulation is provided between the two electrode plates. spacers, and the electrode plates are connected in series through insulating support rods, the quartz tubes stand upright through the electrode plates, and the upper ends of the quartz tubes pass upwards out of the electrolytic cell. Compared with the existing technology, it can make the ultraviolet photochemical oxidation, photocatalytic oxidation and electrocatalytic oxidation treatment technology have a synergistic effect, so that the whole degradation process of sewage is rapid, efficient, simple in structure, easy to maintain, easy to disassemble and assemble, The advantage of low production cost. The invention also discloses an electrode plate used in the photoelectrochemical electrolysis device.

Description

光电化学电解设备及用于该光电化学电解设备的电极板Photoelectrochemical electrolysis device and electrode plate used in the photoelectrochemical electrolysis device

技术领域 technical field

本发明涉及一种污水处理装置,特别是涉及一种将光化学氧化技术、光催化氧化技术和电催化氧化技术于一体并形成协同效应的光电化学电解设备。 The invention relates to a sewage treatment device, in particular to a photoelectrochemical electrolysis device which integrates photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology to form a synergistic effect.

背景技术 Background technique

世界性的环境污染与生态破坏使人们对高效、节能、无二次污染的环境治理技术给予极大的关注。近年来,光催化氧化技术和电催化氧化技术作为有毒或难生物降解的有机污染物的处理方法引起了国内外学者持续的关注,这两种技术都具有结构简单、操作条件容易控制、氧化能力强、无二次污染等优点,成为当前环境污染控制领域中最为活跃的两个研究热点,并显示出广阔的应用前景。 Worldwide environmental pollution and ecological damage have caused people to pay great attention to high-efficiency, energy-saving, and non-secondary pollution environmental governance technologies. In recent years, photocatalytic oxidation technology and electrocatalytic oxidation technology have attracted continuous attention from scholars at home and abroad as treatment methods for toxic or refractory organic pollutants. These two technologies have simple structure, easy control of operating conditions, and oxidation capacity Strong, no secondary pollution and other advantages, become the two most active research hotspots in the field of environmental pollution control, and show broad application prospects.

光催化技术是在半导体光催化剂的作用下,利用光能将污染物分解为无毒或毒性较低的物质的过程。基本原理是:当半导体光催化剂受到能量大于禁带宽度的光照射时,其价带上的电极受到激发,越过禁带进入导带,在价带上留下带正电的空穴,此光生空穴具有极强氧化性,可以夺取水中的电子,生产氧化性很强的羟基自由基,羟基自由基能够对电极表面附近的有机污染物进行无选择性的氧化,而且能发生所谓的“电化学燃烧”过程将有机物彻底氧化为CO2和水;但在实际应用中,光催化氧化过程需要通入电子捕获剂,用于捕获光生电子,才能有效快速氧化降解有机物,常用的电子捕获剂是氧气。 Photocatalytic technology is the process of using light energy to decompose pollutants into non-toxic or less toxic substances under the action of semiconductor photocatalysts. The basic principle is: when the semiconductor photocatalyst is irradiated by light with energy greater than the forbidden band width, the electrode on the valence band is excited, crosses the forbidden band and enters the conduction band, leaving positively charged holes on the valence band. Holes are extremely oxidizing, and can capture electrons in water to produce highly oxidizing hydroxyl radicals. Hydroxyl radicals can non-selectively oxidize organic pollutants near the electrode surface, and can produce the so-called "electrical The chemical combustion” process completely oxidizes organic matter into CO 2 and water; but in practical applications, the photocatalytic oxidation process needs to be fed with an electron capture agent to capture photogenerated electrons, so as to effectively and rapidly oxidize and degrade organic matter. The commonly used electron capture agent is oxygen.

从工程角度出发,光催化处理有机废水通常采用两种反应系统: From an engineering point of view, photocatalytic treatment of organic wastewater usually uses two reaction systems:

一种是悬浮光催化剂水处理系统,即将粉体状光催化剂材料分散于污水中,再施加光辐射,因光催化剂与有机污染物接触面积大,表现出良好的光催化氧化效率,多数情况下可以将有机物彻底矿化。然而,悬浮相粉体材料存在着难以回收、容易中毒等缺点;这些缺点使得该体系难以成为一项实用的技术。 One is the suspended photocatalyst water treatment system, which is to disperse the powdery photocatalyst material in the sewage, and then apply light radiation. Because the photocatalyst has a large contact area with organic pollutants, it shows good photocatalytic oxidation efficiency. In most cases Organic matter can be completely mineralized. However, the suspension phase powder material has disadvantages such as difficult recovery and easy poisoning; these disadvantages make it difficult for this system to become a practical technology.

另一种是固定化系统,即将光催化剂固化到适当载体上,再施加以光辐射,该系统还可借助于外加电场提高光催化反应效率;其原理是:在光催化体系中外加电场可以在光电极内部产生一个电位梯度,使得光生电子在电场作用下迁移到对电极,载流子得以分离,减少“电子-空穴”的重新复合,这样就能在半导体中维持较高的空穴浓度,有利于充分发挥光生空穴的氧化作用,从而提高光催化反应的效率。固定化技术克服了悬浮相体系中光催化剂难回收的缺点,并借助外电场来抑制“电子-空穴”的简单复合,相对来说实用性更强。但负载后催化剂的比表面积减小而带来的量子效应和表面和界面效应减弱等问题仍悬而未决。 The other is the immobilization system, which is to cure the photocatalyst on a suitable carrier and then apply light radiation. This system can also improve the efficiency of the photocatalytic reaction by means of an external electric field; the principle is: in the photocatalytic system, the external electric field can be A potential gradient is generated inside the photoelectrode, so that the photogenerated electrons migrate to the counter electrode under the action of the electric field, the carriers are separated, and the recombination of "electron-holes" is reduced, so that a high hole concentration can be maintained in the semiconductor , which is beneficial to give full play to the oxidation of photogenerated holes, thereby improving the efficiency of photocatalytic reactions. The immobilization technology overcomes the disadvantage that the photocatalyst is difficult to recover in the suspension phase system, and uses an external electric field to suppress the simple recombination of "electron-hole", which is relatively more practical. However, issues such as the quantum effect and the weakening of the surface and interface effects caused by the reduction of the specific surface area of the supported catalyst are still unresolved.

电催化技术是指在外电场的作用下使电极、电解质界面上的电荷转移加速反应的一种催化作用,所选用的电极材料在通电过程中具有催化剂的作用,从而改变电极反应速率或反应方向,而其本身并不发生质的变化;即电催化作用包含电极反应和催化作用两个方面,因此电催化电极必需同时具有这两种功能:①能导电和比较自由地传递电子;②能对反应底物进行有效的催化活化作用。 Electrocatalytic technology refers to a kind of catalysis that accelerates the charge transfer reaction on the electrode and electrolyte interface under the action of an external electric field. The selected electrode material has a catalytic effect during the electrification process, thereby changing the electrode reaction rate or reaction direction. And it does not undergo qualitative changes; that is, the electrocatalysis includes two aspects of electrode reaction and catalysis, so the electrocatalysis electrode must have these two functions at the same time: ① can conduct electricity and transfer electrons relatively freely; ② can react to the reaction substrate for efficient catalytic activation.

在电催化过程必可避免阳极有氧气的析出,在单一的电催化氧化降解有机物中,氧气的析出被认为是副反应,浪费电能;因为阳极电解析出的氧气的氧化能力远不如羟基自由基、双氧水和臭氧,因此,阳极析出的氧气大部分析出到空气中,这就是等于浪费电能。为了抑制析氧副反应的发生,通常采用高析氧过电位的电极材料,如没有电催化活性的二氧化锡/钛基阳极,二氧化铅阳极,或者是掺杂硼的金刚石电极材料;这类材料的析氧过电位高,因此能有效减少析氧副反应发生,提高了电解效率。但这类材料的阳极的使用导致槽压高,实际能耗还是很高,因此并没有根本上解决能耗的问题。另外,电催化主要是将有机物降解成小分子的有机物,很难将有机物彻底降解成二氧化碳和水。 In the electrocatalytic process, the precipitation of oxygen at the anode must be avoided. In the single electrocatalytic oxidation degradation of organic matter, the precipitation of oxygen is considered as a side reaction, which is a waste of electric energy; because the oxidation ability of the oxygen electrolytically separated from the anode is far inferior to that of hydroxyl radicals , hydrogen peroxide and ozone, therefore, most of the oxygen precipitated from the anode is precipitated into the air, which is equal to a waste of electric energy. In order to suppress the occurrence of oxygen evolution side reactions, electrode materials with high oxygen evolution overpotential are usually used, such as tin dioxide/titanium-based anodes without electrocatalytic activity, lead dioxide anodes, or boron-doped diamond electrode materials; this Such materials have a high oxygen evolution overpotential, so they can effectively reduce the occurrence of oxygen evolution side reactions and improve the electrolysis efficiency. However, the use of anodes of this type of material leads to high cell pressure, and the actual energy consumption is still very high, so the problem of energy consumption has not been fundamentally solved. In addition, electrocatalysis is mainly to degrade organic matter into small molecular organic matter, and it is difficult to completely degrade organic matter into carbon dioxide and water.

光化学氧化也是常用的一种有机废水处理方法。光化学氧化是在光的作用下发生的化学反应。光化学反应需要有机分子吸收特定波长的电磁辐射,受激发、产生分子激发态,之后才会发生化学变化到另外一个稳态,或者变成引发热反应的中间化学产物。光化学氧化技术存在以下不足:(1)在紫外光照射下,某些有机物能直接分解成小分子有机物或者是二氧化碳和水,但只能针对少部分有机物才有效,且光降解有机物的效率较低;(2)通常,光化学氧化技术需要加入臭氧、过氧化氢等作为氧化剂,过氧化氢在紫外光照射下能转变成氧化性能更强的羟基自由基,使污染物在紫外光照射下氧化分解。 Photochemical oxidation is also commonly used as an organic wastewater treatment method. Photochemical oxidation is a chemical reaction that occurs under the action of light. Photochemical reactions require organic molecules to absorb electromagnetic radiation of a specific wavelength, to be excited, to generate molecular excited states, and then to undergo chemical changes to another stable state, or to become intermediate chemical products that trigger thermal reactions. Photochemical oxidation technology has the following deficiencies: (1) Under the irradiation of ultraviolet light, some organic substances can be directly decomposed into small molecular organic substances or carbon dioxide and water, but it is only effective for a small part of organic substances, and the efficiency of photodegradation of organic substances is low (2) Usually, photochemical oxidation technology needs to add ozone, hydrogen peroxide, etc. as oxidants, and hydrogen peroxide can be transformed into hydroxyl radicals with stronger oxidation performance under ultraviolet light irradiation, so that pollutants can be oxidized and decomposed under ultraviolet light irradiation .

综上所述,各种方法单一使用时均存在一定的局限性。因此,如何将各氧化技术联合应用并形成协同效应,保证水质处理效果,是当今难降解有机物废水处理的研究方向。 To sum up, each method has certain limitations when used alone. Therefore, how to apply various oxidation technologies together and form a synergistic effect to ensure the effect of water quality treatment is the current research direction for refractory organic wastewater treatment.

现市出上出现了采用光化学氧化和电催化氧化协同处理的装置,如中国发明专利,2004年2月25日公开的公开号为CN1477061A的光电协同高效净化饮用水的技术及装置,其包括有集成的光解电解的一体化反应器、紫外灯、作为电解阳板的网孔材料的内筒筒体和作为电解阴极的反应器的外筒筒体,利用紫外灯发出的紫外光的光解和电极电解的联合作用,通过产生具有协同增效作用的净水效应,可迅速有效降解水中的有机污染物。然而,经实验表明,该装置对污水的处理效果还是不太理想;从实施例二可以看出,该装置对有机碳的去除率以及对五氯酚的处理效果都较低;并受该装置的整体结构限制,存在以下几个技术问题:(1)采用圆筒套圆筒的结构,单个电解槽中能够受到光照的阳极面积受限,仅为圆柱形阳极的内表面;(2)所选用的阳极材料为单一功能的材料,如二氧化钌/钛基电极、二氧化铅/钛基电极为电催化阳极,不具有光催化活性;二氧化钛/钛基电极为惰性电极,具有光催化性能,而不具备电催化活性;(3)阴极采用不锈钢或石墨材料,没有光催化性能;因此公开号为CN1477061A的专利所公开的该设备的处理效果略差。 Devices that adopt photochemical oxidation and electrocatalytic oxidation synergistic treatment have appeared in the market, such as the Chinese invention patent, the publication number of which was published on February 25, 2004 is the technology and device of photoelectric synergy and efficient purification of drinking water of CN1477061A, which includes Integrated photolysis and electrolysis integrated reactor, ultraviolet lamp, inner cylinder as the mesh material of the electrolysis positive plate and the outer cylinder of the reactor as the electrolysis cathode, the photolysis of the ultraviolet light emitted by the ultraviolet lamp The combined effect of electrolysis and electrode electrolysis can quickly and effectively degrade organic pollutants in water by producing a synergistic water purification effect. Yet, show through experiment, this device is still unsatisfactory to the treatment effect of sewage; As can be seen from embodiment two, this device is all lower to the removal rate of organic carbon and to the treatment effect of pentachlorophenol; Due to the limitation of the overall structure, there are several technical problems as follows: (1) With the structure of a cylinder inside a cylinder, the area of the anode that can be illuminated in a single electrolytic cell is limited, only the inner surface of the cylindrical anode; (2) The anode material selected is a material with a single function, such as ruthenium dioxide/titanium-based electrodes, lead dioxide/titanium-based electrodes are electrocatalytic anodes, which do not have photocatalytic activity; titanium dioxide/titanium-based electrodes are inert electrodes, which have photocatalytic properties , without electrocatalytic activity; (3) the cathode adopts stainless steel or graphite material, which has no photocatalytic performance; therefore, the treatment effect of the device disclosed in the patent of CN1477061A is slightly worse.

有鉴于此,本发明人对上述问题进行深入研究,遂于本案产生。 In view of this, the inventor conducted in-depth research on the above-mentioned problem, and then produced this case.

发明内容 Contents of the invention

本发明的目的在于提供一种光电化学电解设备,其可将光化学氧化技术、光催化氧化技术和电催化氧化技术于一体,并使之形成协同效应,具有降解速度快,效率高,结构简易的优点。 The purpose of the present invention is to provide a photoelectrochemical electrolysis equipment, which can integrate photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology, and make them form a synergistic effect, with fast degradation speed, high efficiency and simple structure advantage.

本发明的另一目的在于提供一种用于该光电化学电解设备的电极板,其与紫外灯配合使用时能够实现将光化学氧化技术、光催化氧化技术和电催化氧化技术于一体,并使之形成协同效应,对污水的降解速度快,且效率高。 Another object of the present invention is to provide an electrode plate for the photoelectrochemical electrolysis equipment, which can realize the integration of photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology when used in conjunction with ultraviolet lamps, and make it A synergistic effect is formed, and the degradation speed of sewage is fast and the efficiency is high.

为了达成上述目的,本发明的解决方案是: In order to achieve the above object, the solution of the present invention is:

光电化学电解设备,包括电解槽及设于电解槽内的石英管、紫外灯和电极板,该紫外灯竖立于该石英管内,该电解槽上设置有污水进口和处理水出口;上述电极板设置有若干片,各电极板平放设置,并呈由上而下间隔排列,每一电极板具有对半设置的阳极部和阴极部,上述电极板的第一半部位表面上涂覆有具有电催化活性的金属氧化物涂层,此电极板的第一半部位为上述阳极部,上述电极板的第二半部位的表面涂覆有具有光催化活性的半导体光催化剂涂层,上述电极板的第二半部位为上述阴极部;上下设置的两电极板中处于上方的电极板的阳极部与处于下方的电极板的阴极部呈上下相对设置,两电极板之间均设置有绝缘间隔件,且各电极板通过绝缘支撑杆串接在一起,上述石英管竖立穿过各上述电极板,并与上述电极板套紧配合,且上述石英管的上端端部向上穿出上述电解槽外。 Photoelectrochemical electrolysis equipment, including an electrolytic cell and a quartz tube arranged in the electrolytic cell, an ultraviolet lamp and an electrode plate, the ultraviolet lamp is erected in the quartz tube, and the electrolytic cell is provided with a sewage inlet and a treated water outlet; There are several sheets, and each electrode plate is placed flat and arranged at intervals from top to bottom. Each electrode plate has an anode part and a cathode part set in half, and the surface of the first half of the above electrode plate is coated with a Catalytically active metal oxide coating, the first half of the electrode plate is the above-mentioned anode part, the surface of the second half of the above-mentioned electrode plate is coated with a semiconductor photocatalyst coating with photocatalytic activity, the surface of the above-mentioned electrode plate The second half is the above-mentioned cathode part; among the two electrode plates arranged up and down, the anode part of the upper electrode plate and the cathode part of the lower electrode plate are vertically opposite to each other, and an insulating spacer is arranged between the two electrode plates. And the electrode plates are connected in series through insulating support rods, the above-mentioned quartz tubes stand upright through each of the above-mentioned electrode plates, and are tightly fitted with the above-mentioned electrode plates, and the upper ends of the above-mentioned quartz tubes go out of the above-mentioned electrolytic cell upwards.

上述石英管设置有若干个,上述紫外灯相应设置有若干个,并与上述石英管一一相对应设置,各上述紫外灯通过导线与外界电源电连接。 There are several above-mentioned quartz tubes, and several above-mentioned ultraviolet lamps are arranged correspondingly to the above-mentioned quartz tubes one by one. Each of the above-mentioned ultraviolet lamps is electrically connected to an external power supply through wires.

上述电极板为网孔板。 The above-mentioned electrode plate is a mesh plate.

上述电极板为金属钛板,上述金属氧化物涂层为含有RuO2的复合金属氧化物涂层或者含有IrO2的多元氧化物涂层,上述半导体光催化剂涂层为Cu2O、ZnO、SnO2、TiO2中的一种氧化物涂层,或者,上述半导体光催化剂涂层为Cu2O、ZnO、SnO2、TiO2中的两种或两种以上氧化物组成的复合涂层。 The above-mentioned electrode plate is a metal titanium plate, the above-mentioned metal oxide coating is a composite metal oxide coating containing RuO2 or a multi-component oxide coating containing IrO2 , and the above-mentioned semiconductor photocatalyst coating is Cu2O, ZnO, SnO 2. An oxide coating in TiO 2 , or the semiconductor photocatalyst coating is a composite coating composed of two or more oxides in Cu 2 O, ZnO, SnO 2 , and TiO 2 .

上述复合金属氧化物涂层为RuO2-TiO2复合金属氧化物涂层、RuO2-TiO2-SnO2复合金属氧化物涂层、RuO2-SnO2复合金属氧化物涂层、RuO2-Ta2O5复合氧化物涂层中的一种;上述多元氧化物涂层为IrO2-TiO2二元氧化物涂层、IrO2-TiO2-SnO2三元氧化物涂层、IrO2-SnO2二元氧化物涂层、IrO2-Ta2O2二元氧化物涂层中的一种。 The above composite metal oxide coatings are RuO 2 -TiO 2 composite metal oxide coatings, RuO 2 -TiO 2 -SnO 2 composite metal oxide coatings, RuO 2 -SnO 2 composite metal oxide coatings, RuO 2 - One of Ta 2 O 5 composite oxide coatings; the above multi-component oxide coatings are IrO 2 -TiO 2 binary oxide coatings, IrO 2 -TiO 2 -SnO 2 ternary oxide coatings, IrO 2 - one of SnO 2 binary oxide coating and IrO 2 -Ta 2 O 2 binary oxide coating.

上述电解槽呈方形结构,上述电解槽呈其上下两端为敞开状的中空结构,上述电解槽的上端端面锁固有密封电解槽上端开口的上密封盖,上述上密封盖上具有与电解槽的中空腔室相通的出水管,上述石英管的上端端部紧密穿出上密封盖外;上述电解槽的下端端面锁固有密封电解槽下端开口的下密封盖,上述下密封盖上具有与电解槽的中空腔室相通的进水管。 The above-mentioned electrolytic cell has a square structure, and the above-mentioned electrolytic cell has a hollow structure with open upper and lower ends. The upper end face of the above-mentioned electrolytic cell is locked with an upper sealing cover that seals the upper opening of the electrolytic cell. The outlet pipe connected to the hollow chamber, the upper end of the above-mentioned quartz tube tightly passes through the upper sealing cover; the lower end face of the above-mentioned electrolytic cell is locked with a lower sealing cover that seals the lower opening of the electrolytic cell, and the above-mentioned lower sealing cover has a The hollow chamber communicates with the water inlet pipe.

上述上密封盖和下密封盖均为金属钛盖板,上述上密封盖与上述下密封盖相对的对立面上涂覆有一层具有电催化活性的金属氧化物涂层,上述上密封盖和下密封盖分别对应与外部直流电源的正、负极电连接。 The above-mentioned upper sealing cover and the lower sealing cover are metal titanium cover plates, and the opposite surface of the above-mentioned upper sealing cover and the above-mentioned lower sealing cover is coated with a layer of metal oxide coating with electrocatalytic activity, and the above-mentioned upper sealing cover and the lower sealing cover The covers are respectively electrically connected to the positive and negative poles of the external DC power supply.

上述石英管与上述上密封盖之间通过套装在石英管外的密封套进行密封,上述上密封盖上开设有供密封套穿过的安装孔,上述密封套嵌装于上述安装孔内,且密封套的外侧壁凹设有供安装孔的孔沿紧密伸入于内的安装凹槽。 The above-mentioned quartz tube and the above-mentioned upper sealing cover are sealed by a sealing sleeve set outside the quartz tube, and the above-mentioned upper sealing cover is provided with an installation hole for the sealing sleeve to pass through, and the above-mentioned sealing sleeve is embedded in the above-mentioned installation hole, and The outer wall of the sealing sleeve is concavely provided with a mounting groove for the hole edge of the mounting hole to tightly extend inside.

上述支撑间隔件呈中空圆柱状结构,上述支撑间隔件的上、下两端端部外侧壁上分别向外凸设有叠设于电极板上下两面的支撑环。 The support spacer has a hollow cylindrical structure, and the outer walls of the upper and lower ends of the support spacer are respectively protruding outwards with support rings stacked on the upper and lower sides of the electrode plate.

一种用于光电化学电解设备的电极板,包括电极板本体,上述电极板本体具有对半设置的阳极部和阴极部,上述电极板本体的第一半部位表面上涂覆有具有电催化活性的金属氧化物涂层,此电极板本体的第一半部位为上述阳极部,上述电极板本体的第二半部位的表面涂覆有具有光催化活性的半导体光催化剂涂层,上述电极板本体的第二半部位为上述阴极部。 An electrode plate for photoelectrochemical electrolysis equipment, comprising an electrode plate body, the electrode plate body has an anode part and a cathode part set in half, and the surface of the first half of the electrode plate body is coated with electrocatalytic activity The metal oxide coating, the first half of the electrode plate body is the anode part, the surface of the second half of the electrode plate body is coated with a semiconductor photocatalyst coating with photocatalytic activity, the electrode plate body The second half of the part is the above-mentioned cathode part.

上述电极板本体为多孔结构。 The above-mentioned electrode plate body has a porous structure.

上述电极板本体为网孔板,上述网孔板上设置有若干个圆形穿孔。 The above-mentioned electrode plate body is a mesh plate, and several circular perforations are arranged on the above-mentioned mesh plate.

上述电极板本体为金属钛板,上述金属氧化物涂层为含有RuO2的复合金属氧化物涂层或者含有IrO2的多元氧化物涂层,上述半导体光催化剂涂层为Cu2O、ZnO、SnO2、TiO2中的一种氧化物涂层,或者,上述半导体光催化剂涂层为Cu2O、ZnO、SnO2、TiO2中的两种或两种以上氧化物组成的复合涂层。 The above-mentioned electrode plate body is a metal titanium plate, the above-mentioned metal oxide coating is a composite metal oxide coating containing RuO2 or a multi-component oxide coating containing IrO2 , and the above - mentioned semiconductor photocatalyst coating is Cu2O, ZnO, An oxide coating of SnO 2 and TiO 2 , or, the semiconductor photocatalyst coating is a composite coating composed of two or more oxides of Cu 2 O, ZnO, SnO 2 and TiO 2 .

上述复合金属氧化物涂层为RuO2-TiO2复合金属氧化物涂层、RuO2-TiO2-SnO2复合金属氧化物涂层、RuO2-SnO2复合金属氧化物涂层、RuO2-Ta2O5复合氧化物涂层中的一种;上述多元氧化物涂层为IrO2-TiO2二元氧化物涂层、IrO2-TiO2-SnO2三元氧化物涂层、IrO2-SnO2二元氧化物涂层、IrO2-Ta2O2二元氧化物涂层中的一种。 The above composite metal oxide coatings are RuO 2 -TiO 2 composite metal oxide coatings, RuO 2 -TiO 2 -SnO 2 composite metal oxide coatings, RuO 2 -SnO 2 composite metal oxide coatings, RuO 2 - One of Ta 2 O 5 composite oxide coatings; the above multi-component oxide coatings are IrO 2 -TiO 2 binary oxide coatings, IrO 2 -TiO 2 -SnO 2 ternary oxide coatings, IrO 2 - one of SnO 2 binary oxide coating and IrO 2 -Ta 2 O 2 binary oxide coating.

采用上述技术方案后,本发明的光电化学电解设备的有益效果如下: After adopting above-mentioned technical scheme, the beneficial effect of photoelectrochemical electrolysis equipment of the present invention is as follows:

(1)、因电极板的一半为阳极部,另一半为阳极部,上下两电极板中处于上方的电极板的阳极部与处于下方的电板板的阴板部相对设置,则两阴极部之间设置有一阳极部,石英管穿过各电极板,这样,两电极板之间所形成的区域均具有阴极电解区域、阳极电解区域和紫外光照射区域,可将阳极析氧副反应转化为有效反应,同时克服电催化氧化或光催化氧化单一技术存在的缺点,并形成优势互补,使光化学氧化技术、光催化氧化技术和电催化氧化技术的协同效用作用佳,从而使污水的整一降解过程迅速,高效; (1), because half of the electrode plate is the anode part, and the other half is the anode part, and the anode part of the upper electrode plate in the upper and lower two electrode plates is arranged opposite to the negative plate part of the lower electric plate, then the two cathode parts There is an anode part between them, and the quartz tube passes through each electrode plate. In this way, the area formed between the two electrode plates has a cathode electrolysis area, an anode electrolysis area and an ultraviolet light irradiation area, which can convert the anodic oxygen evolution side reaction into Effective reaction, at the same time overcome the shortcomings of electrocatalytic oxidation or photocatalytic oxidation single technology, and form complementary advantages, so that the synergistic effect of photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology is good, so that the whole sewage can be degraded The process is fast and efficient;

(2)石英管贯穿各电极板,则各电极板的正反面均能被紫外光辐照,光催化氧化的效果较佳; (2) The quartz tube runs through each electrode plate, so the front and back of each electrode plate can be irradiated by ultraviolet light, and the effect of photocatalytic oxidation is better;

(3)各电极板之间的距离可任意调节,即上下阴阳极之间的距离能够任意调节,这样,可通过减小两电极之间的距离来有效降低电解槽的槽压,能耗小,节能;并可根据实际情况有效地调整电极板的数量,以满足实际情况中不同污水处理场合的需要;适应性强; (3) The distance between the electrode plates can be adjusted arbitrarily, that is, the distance between the upper and lower cathodes and anodes can be adjusted arbitrarily, so that the tank pressure of the electrolytic cell can be effectively reduced by reducing the distance between the two electrodes, and the energy consumption is small , energy saving; and the number of electrode plates can be effectively adjusted according to the actual situation to meet the needs of different sewage treatment occasions in the actual situation; strong adaptability;

(4)电极板上同时赋予电催化活性的阳极区域和光催化活性的阴极区域,使电子可以直接通过电极板传导,无需通过外部导线传输,降低了电子传输过程的电阻,即光生“电子-空穴“对的分离更为顺畅,光生“电子-空穴”对的分离效果越好,生成强氧化性的羟基自由基的能力越强。 (4) The electrode plate is endowed with an electrocatalytically active anode area and a photocatalytically active cathode area at the same time, so that electrons can be directly conducted through the electrode plate without being transmitted through external wires, which reduces the resistance of the electron transfer process, that is, the photogenerated "electron-air" The smoother the separation of "hole" pairs, the better the separation effect of photogenerated "electron-hole" pairs, and the stronger the ability to generate strong oxidizing hydroxyl radicals.

采用上述技术方案后,本发明的用于光电化学电解设备的电极板,由于电极板本体上同时赋予电催化活性的阳极区域和光催化活性的阴极区域,则此电极板本体与紫外灯管配合使用时能够实现将光化学氧化技术、光催化氧化技术和电催化氧化技术于一体,并使之形成协同效应,对污水的降解过程快速,并高效;同时,可使电子可以直接通过电极板本体传导,无需通过外部导线传输,降低了电子传输过程的电阻,即光生“电子-空穴“对的分离更为顺畅,光生“电子-空穴”对的分离效果越好,生成强氧化性的羟基自由基的能力越强。 After adopting the above-mentioned technical scheme, the electrode plate used for photoelectrochemical electrolysis equipment of the present invention, since the anode area of electrocatalytic activity and the cathode area of photocatalytic activity are simultaneously provided on the electrode plate body, the electrode plate body is used in conjunction with the ultraviolet lamp At the same time, it can realize the integration of photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology, and make them form a synergistic effect, and the degradation process of sewage is fast and efficient; at the same time, electrons can be directly conducted through the electrode plate body, It does not need to be transmitted through external wires, which reduces the resistance of the electron transport process, that is, the separation of photogenerated "electron-hole" pairs is smoother, and the separation effect of photogenerated "electron-hole" pairs is better, generating strong oxidizing hydroxyl radicals. The base is stronger.

附图说明 Description of drawings

图1为光电化学电解设备的立体图; Fig. 1 is the perspective view of photoelectrochemical electrolysis equipment;

图2为电极板与石英管的组装示意图; Fig. 2 is the assembly schematic diagram of electrode plate and quartz tube;

图3为电极板与石英管的组装立体图 Figure 3 is a perspective view of the assembly of the electrode plate and the quartz tube

图4为石英管与上密封盖的组装示意图; Fig. 4 is the schematic diagram of the assembly of quartz tube and upper sealing cover;

图5为电极板的示意图。 Fig. 5 is a schematic diagram of an electrode plate.

具体实施方式 detailed description

本发明的用于光电化学电解设备的电极板4,如图5所示,包括电极板本体,此电极板本体具有对半设置的阳极部4a和阴极部4b,电极板4为金属钛板,电极板4的第一半部位表面上涂覆有具有电催化活性的金属氧化物涂层(图中未示出),此金属氧化物涂层为含有RuO2的复合金属氧化物涂层,此复合金属氧化物涂层为RuO2-TiO2复合金属氧化物涂层、RuO2-TiO2-SnO2复合金属氧化物涂层、RuO2-SnO2复合金属氧化物涂层、RuO2-Ta2O5复合氧化物涂层中的一种;此电极板的第一半部位即可构成所述阳极部4a,电极板4的第二半部位的表面涂覆有具有光催化活性的半导体光催化剂涂层(图中未示出),半导体光催化剂涂层为Cu2O、ZnO、SnO2、TiO2中的一种氧化物涂层,即电极板的第二半部位即可构成所述阴极部4b。本实施例中,半导体光催化剂涂层也可为由Cu2O、ZnO、SnO2、TiO2中的两种或两种以上氧化物组成的复合涂层;金属氧化物涂层也可为含有IrO2的多元氧化物涂层,此多元氧化物涂层为IrO2-TiO2二元氧化物涂层、IrO2-TiO2-SnO2三元氧化物涂层、IrO2-SnO2二元氧化物涂层、IrO2-Ta2O2二元氧化物涂层中的一种。 The electrode plate 4 for photoelectrochemical electrolysis equipment of the present invention, as shown in Figure 5, comprises electrode plate body, and this electrode plate body has anode portion 4a and cathode portion 4b that are arranged in half, and electrode plate 4 is metal titanium plate, The surface of the first half of the electrode plate 4 is coated with an electrocatalytically active metal oxide coating (not shown), this metal oxide coating is a composite metal oxide coating containing RuO 2 , this The composite metal oxide coating is RuO 2 -TiO 2 composite metal oxide coating, RuO 2 -TiO 2 -SnO 2 composite metal oxide coating, RuO 2 -SnO 2 composite metal oxide coating, RuO 2 -Ta One of the 2 O 5 composite oxide coatings; the first half of the electrode plate can constitute the anode part 4a, and the surface of the second half of the electrode plate 4 is coated with photocatalytically active semiconductor light Catalyst coating (not shown in the figure), the semiconductor photocatalyst coating is an oxide coating in Cu 2 O, ZnO, SnO 2 , TiO 2 , that is, the second half of the electrode plate can constitute the Cathode part 4b. In this embodiment, the semiconductor photocatalyst coating can also be a composite coating composed of two or more oxides in Cu 2 O, ZnO, SnO 2 , TiO 2 ; the metal oxide coating can also be a composite coating containing IrO 2 multi-element oxide coating, this multi-element oxide coating is IrO 2 -TiO 2 binary oxide coating, IrO 2 -TiO 2 -SnO 2 ternary oxide coating, IrO 2 -SnO 2 binary One of oxide coating and IrO 2 -Ta 2 O 2 binary oxide coating.

本发明的电极板4,其上同时赋予电催化活性的阳极区域和光催化活性的阴极区域,则此电极板与紫外灯管配合使用时用于处理污水时能够实现将光化学氧化技术、光催化氧化技术和电催化氧化技术于一体,并使之形成协同效应,对污水的降解过程快速,并高效;同时,在使用时,可使电子可以直接通过电极板本体传导,无需通过外部导线传输,降低了电子传输过程的电阻,即光生“电子-空穴“对的分离更为顺畅,光生“电子-空穴”对的分离效果越好,生成强氧化性的羟基自由基的能力越强。 The electrode plate 4 of the present invention is endowed with an electrocatalytically active anode region and a photocatalytically active cathode region at the same time, and when the electrode plate is used in conjunction with an ultraviolet lamp tube for treating sewage, it can realize the combination of photochemical oxidation technology, photocatalytic oxidation Technology and electrocatalytic oxidation technology are integrated to form a synergistic effect, and the degradation process of sewage is fast and efficient; at the same time, when in use, electrons can be directly conducted through the body of the electrode plate without transmission through external wires, reducing The resistance of the electron transport process is improved, that is, the separation of photogenerated "electron-hole" pairs is smoother, and the better the separation effect of photogenerated "electron-hole" pairs, the stronger the ability to generate strong oxidizing hydroxyl radicals.

本发明中,此电极板本体为多孔结构,优选的是采用网孔板,利用电极板4的网孔可供污水穿过电极板4,这样,一方面可使污水与电极板得到有效接触,且污水与电极板的有效接触程序越高,污水被降解的效率则越高;另一方面能保证污水的顺利流通。 In the present invention, the electrode plate body is a porous structure, preferably a mesh plate, and the mesh of the electrode plate 4 can be used for sewage to pass through the electrode plate 4. In this way, on the one hand, the sewage can be effectively contacted with the electrode plate, Moreover, the higher the effective contact procedure between sewage and electrode plates, the higher the efficiency of sewage degradation; on the other hand, it can ensure the smooth circulation of sewage.

本发明中,此网孔板上设置有若干个圆形穿孔41,利用此圆形穿孔41可供紫外灯管的安装,实现紫外灯管与电极板的串接配合,且紫外灯管与电极板的串接配合可使电极板4的正反面均能被紫外光辐照,光催化氧化的效果较佳。 In the present invention, the mesh plate is provided with several circular perforations 41, and the circular perforations 41 can be used for the installation of ultraviolet lamps, so as to realize the serial connection and cooperation of ultraviolet lamps and electrode plates, and the ultraviolet lamps and electrodes The series connection of the plates can make both the front and back of the electrode plate 4 irradiated by ultraviolet light, and the effect of photocatalytic oxidation is better.

本发明的光电化学电解设备,如图1-4所示,包括电解槽1、石英管2、紫外灯3和电极板4,其中: Photoelectrochemical electrolysis equipment of the present invention, as shown in Figure 1-4, comprises electrolyzer 1, quartz tube 2, ultraviolet lamp 3 and electrode plate 4, wherein:

电解槽1上设有置有污水进口和处理水出口,此电解槽1的优选结构是:该电解槽1呈方形结构,电解槽呈其上下两端为敞开状的中空结构,电解槽1的上端端面锁固密封电解槽1上端开口的上密封盖5,上密封盖5通过螺栓51与螺母52的配合与电解槽1可拆卸锁固在一起,即电解槽1的上端端部周沿凸设有与上密封盖5的外周沿相叠配合的上安装环11,此上安装环11与上密封盖5通过此螺栓51与螺母52的配合锁固在一起;该电解槽1的下端端面锁固有密封电解槽1下端开口的下密封盖6,下密封盖6通过螺栓61与螺母62的配合与电解槽1可拆卸锁固在一起,即电解槽1的下端端部周沿凸设有与下密封盖6的外周沿相叠配合的下安装环12,此下安装环12与下密封盖6通过此螺栓61与螺母62的配合锁固在一起;该上密封盖5的上表面上固定竖立有与电解槽1的中空腔室相通的出水管53,此出水管53即为处理水出口,该下密封盖6的下底面固定竖立有与电解槽1的中空腔室相通的进水管63,此进水管63即为污水进口。 The electrolytic cell 1 is provided with a sewage inlet and a treated water outlet. The preferred structure of the electrolytic cell 1 is: the electrolytic cell 1 is a square structure, and the electrolytic cell is a hollow structure with its upper and lower ends open. The upper end face locks and seals the upper sealing cover 5 of the upper opening of the electrolytic cell 1. The upper sealing cover 5 is detachably locked together with the electrolytic cell 1 through the cooperation of the bolt 51 and the nut 52, that is, the upper end of the electrolytic cell 1 is convex along the periphery. There is an upper mounting ring 11 overlapping with the outer periphery of the upper sealing cover 5, and the upper mounting ring 11 and the upper sealing cover 5 are locked together through the cooperation of the bolt 51 and the nut 52; the lower end surface of the electrolytic cell 1 The lock has a lower sealing cover 6 that seals the opening of the lower end of the electrolytic cell 1, and the lower sealing cover 6 is detachably locked together with the electrolytic cell 1 through the cooperation of the bolt 61 and the nut 62, that is, the lower end of the electrolytic cell 1 is convexly arranged on the periphery. The lower mounting ring 12 that overlaps and cooperates with the outer periphery of the lower sealing cover 6, the lower mounting ring 12 and the lower sealing cover 6 are locked together by the cooperation of the bolt 61 and the nut 62; on the upper surface of the upper sealing cover 5 A water outlet pipe 53 communicated with the hollow chamber of the electrolytic cell 1 is fixedly erected, and the outlet pipe 53 is the outlet of the treated water. The lower bottom surface of the lower sealing cover 6 is fixedly erected with a water inlet pipe communicated with the hollow chamber of the electrolytic cell 1 63, this water inlet pipe 63 is the sewage inlet.

该石英管2和紫外灯3均设置有若干,各石英管2与各紫外灯3一一对应设置,紫外灯3竖立于该石英管2内,所述的电极板4采用的是本具体实施方式中所描述的用于光电化学电解设备的电极板,在此不再累述,该电极板4设置有若干片,各电极板4平放设置,并呈由上而下间隔排列,而且,上下设置的两电极板4中处于上方的电极板4的阳极部4a与处于下方的电极板4的阴极部4b呈上下相对设置,两电极板4的两阳极部4a呈上下错位设置,两阴极部4b相应也呈上下错位设置。 This quartz tube 2 and ultraviolet lamp 3 are all provided with several, and each quartz tube 2 and each ultraviolet lamp 3 are arranged one by one, and ultraviolet lamp 3 is erected in this quartz tube 2, and what described electrode plate 4 adopts this embodiment The electrode plates used for photoelectrochemical electrolysis equipment described in the method are not repeated here. The electrode plates 4 are provided with several sheets, and each electrode plate 4 is placed flat and arranged at intervals from top to bottom, and, Among the two electrode plates 4 arranged up and down, the anode portion 4a of the upper electrode plate 4 and the cathode portion 4b of the lower electrode plate 4 are vertically opposite to each other, and the two anode portions 4a of the two electrode plates 4 are dislocated up and down. Correspondingly, the portion 4b is also arranged in an up-and-down dislocation.

两电极板4之间设有绝缘间隔件7,优选的是:绝缘间隔件7呈中空圆柱状结构,绝缘间隔件7竖立设置,通过绝缘间隔件7使各电极板间隔分开,绝缘间隔件7的上下两端端部外侧壁分别向外凸设有闭环形支撑环71,利用此支撑环71可方便电极板4的放置安装,各电极板4通过绝缘支撑杆8串接在一起,即,绝缘支撑杆8穿过各绝缘间隔件7,并与绝缘支撑杆8与电极板4套紧配合,电极板4上开设有供绝缘支撑杆8紧配合穿过的穿孔42,利用绝缘支撑杆8与电极板4的套紧配合可实现各电极板4的固定安装。 An insulating spacer 7 is arranged between the two electrode plates 4, preferably: the insulating spacer 7 is a hollow cylindrical structure, the insulating spacer 7 is erected, and each electrode plate is separated by the insulating spacer 7, and the insulating spacer 7 The outer sidewalls of the upper and lower ends of the upper and lower ends protrude outward respectively and are provided with a closed ring support ring 71, which can facilitate the placement and installation of the electrode plates 4, and the electrode plates 4 are connected in series through the insulating support rods 8, that is, Insulation support rods 8 pass through each insulation spacer 7, and tightly fit with insulation support rods 8 and electrode plates 4. Electrode plates 4 are provided with perforations 42 for the insulation support rods 8 to fit tightly through. The tight cooperation with the electrode plates 4 can realize the fixed installation of each electrode plate 4 .

每一石英管2均穿过各电极板4,且石英管2的下端端部与下密封盖6相抵靠配合,石英管2的上端端部紧配合穿过上密封盖5外,且石英管2与上密封盖5之间通过嵌装在石英管2外的密封套21进行密封配合,具体的是:上密封盖5上开设有供密封套21穿过的安装孔,密封套21嵌装于此安装孔内,且密封套2的外侧壁凹设有供安装孔的孔沿紧密伸入于内的安装凹槽,利用安装凹槽与安装孔孔沿的配合可实现石英管2与上密封盖5的密封配合,该紫外灯3上连接有伸出石英管2的导线100,各紫外灯3的导线100与外界电源电连接。 Each quartz tube 2 passes through each electrode plate 4, and the lower end of the quartz tube 2 abuts against the lower sealing cover 6, and the upper end of the quartz tube 2 tightly fits through the upper sealing cover 5, and the quartz tube 2 and the upper sealing cover 5 are sealed and matched through the sealing sleeve 21 embedded outside the quartz tube 2, specifically: the upper sealing cover 5 is provided with an installation hole for the sealing sleeve 21 to pass through, and the sealing sleeve 21 is embedded In this mounting hole, and the outer side wall of the sealing sleeve 2 is provided with a mounting groove for the hole edge of the mounting hole to extend into the inside tightly, and the quartz tube 2 and the upper With the sealing fit of the sealing cover 5, the ultraviolet lamp 3 is connected with a wire 100 protruding from the quartz tube 2, and the wire 100 of each ultraviolet lamp 3 is electrically connected with an external power supply.

本发明的光电化学电解设备,其工作机理是: Photoelectrochemical electrolysis equipment of the present invention, its operating mechanism is:

电极板4的阴极部4b的二氧化钛层受紫外光照激发,得到光生电子e-和光生空穴h+,反应方程如下, The titanium dioxide layer of the cathode portion 4b of the electrode plate 4 is excited by ultraviolet light to obtain photogenerated electrons e- and photogenerated holes h+, and the reaction equation is as follows,

电极板4的阳极部4a通电析出氧气后,氧气上浮必然与阳极部4a上方的阴极部4b接触。在阴极表面捕获光生电子,生成超氧离子O2 -,反应方程如下, After the anode part 4a of the electrode plate 4 is energized to precipitate oxygen, the oxygen floats up and must contact the cathode part 4b above the anode part 4a. Capture photogenerated electrons on the cathode surface to generate superoxide ions O 2 - , the reaction equation is as follows,

O2+e-→O2 -(2) O 2 +e - → O 2 - (2)

超氧离子O2 -进一步与氢离子反应,生产双氧水,反应方程如下, Superoxide ion O 2 - further reacts with hydrogen ions to produce hydrogen peroxide, and the reaction equation is as follows,

O2 -+2H+→H2O2(3) O 2 - +2H + →H 2 O 2 (3)

双氧水被紫外线照射后生成氧化性能更强的羟基自由基(.OH),反应方程如下, Hydrogen peroxide is irradiated by ultraviolet rays to generate hydroxyl radicals (.OH) with stronger oxidation performance. The reaction equation is as follows,

光生电子被氧捕获后,有效抑制了光生“电子-空穴”对的复合。光生空穴与氢氧根离子反应,生成强氧化性的羟基自由基,反应方程如下, After the photogenerated electrons are captured by oxygen, the recombination of photogenerated "electron-hole" pairs is effectively inhibited. Photogenerated holes react with hydroxide ions to generate strong oxidizing hydroxyl radicals. The reaction equation is as follows,

OH-+h+=·OH(5) OH - +h + =·OH(5)

上述方程式(1)、(5)是光催化过程;方程(2)(3)是光催化与电催化的协同作用过程;方程(4)是光化学反应与光催化和电催化三者协同的具体表现,由此可知,本发明的电解设备可实现光化学氧化技术、光催化氧化技术和电催化氧化技术集成于一体,且三者之间进行协同作用。 The above equations (1), (5) are the photocatalytic process; equations (2) (3) are the synergistic process of photocatalysis and electrocatalysis; It can be seen from this that the electrolysis equipment of the present invention can realize the integration of photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology, and the synergistic effect between the three.

本发明的光电化学电解设备,具有如下有益效果: The photoelectrochemical electrolysis device of the present invention has the following beneficial effects:

(1)、可将光化学氧化技术、光催化氧化技术和电催化氧化技术集成于一体,并可使阳极析氧副反应转化为有效反应,克服电催化氧化或光催化氧化单一技术存在的缺点,并形成优势互补,使光化学氧化技术、光催化氧化技术和电催化氧化技术的协同效用作用佳,从而使污水的整一降解过程迅速,高效; (1) Photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology can be integrated, and the anodic side reaction of oxygen evolution can be converted into an effective reaction, overcoming the shortcomings of electrocatalytic oxidation or photocatalytic oxidation single technology, And form complementary advantages, so that the synergistic effect of photochemical oxidation technology, photocatalytic oxidation technology and electrocatalytic oxidation technology is good, so that the whole degradation process of sewage is rapid and efficient;

(2)石英管2贯穿各电极板4,则各电极板4的正反面均能被紫外光辐照,光催化氧化的效果较佳; (2) The quartz tube 2 runs through each electrode plate 4, so that the front and back surfaces of each electrode plate 4 can be irradiated by ultraviolet light, and the effect of photocatalytic oxidation is better;

(3)各电极板4之间的距离可任意调节,即上下阴阳极之间的距离能够任意调节,这样,可通过减小两电极之间的距离来有效降低电解槽的槽压(因阴、阳极之间的距离越小,处于阴阳极之间的污水的欧姆将越低,则在相同电流密度下工作,槽压越低),能耗小,节能;并可根据实际情况有效地调整电极板的数量,以满足实际情况中不同污水处理场合的需要;适应性强; (3) The distance between each electrode plate 4 can be adjusted arbitrarily, that is, the distance between the upper and lower cathodes and anodes can be adjusted arbitrarily, so that the cell pressure of the electrolytic cell can be effectively reduced by reducing the distance between the two electrodes (due to the cathode , the smaller the distance between the anodes, the lower the ohm of the sewage between the cathode and the anode will be, then work at the same current density, the lower the tank pressure), the energy consumption is small, and energy saving; and can be effectively adjusted according to the actual situation The number of electrode plates to meet the needs of different sewage treatment occasions in the actual situation; strong adaptability;

(4)电极板上同时赋予电催化活性的阳极区域和光催化活性的阴极区域,使电子可以直接通过电极板传导,无需通过外部导线传输,降低了电子传输过程的电阻,即光生“电子-空穴“对的分离更为顺畅,光生“电子-空穴”对的分离效果越好,生成强氧化性的羟基自由基的能力越强。 (4) The electrode plate is endowed with an electrocatalytically active anode area and a photocatalytically active cathode area at the same time, so that electrons can be directly conducted through the electrode plate without being transmitted through external wires, which reduces the resistance of the electron transfer process, that is, the photogenerated "electron-air" The smoother the separation of "hole" pairs, the better the separation effect of photogenerated "electron-hole" pairs, and the stronger the ability to generate strong oxidizing hydroxyl radicals.

(5)、具有结构简易,易维护,拆装方便,制作成本低的优点。 (5) It has the advantages of simple structure, easy maintenance, convenient disassembly and assembly, and low manufacturing cost.

本发明中,上密封盖5和下密封盖6均为金属钛盖板,上密封盖5与下密封盖6相对的对立面上涂覆有一层具有电催化活性的金属氧化物涂层,且上密封盖5和下密封盖6分别对应与外部直流电源的正、负极电连接,这样,利用金属钛的特性与金属氧化物涂层的导电特性使上、下密封盖6、6不论是作为阳极还是阴极使用都具有导电性,则,在连接外部直流电源时,若上密封盖5连接外部直流电源正极,则下密封盖6则连接负极;若上密封盖5连接外部直流电源的负极,则下密封盖6连接正极;使得本发明的光电化学电解设备在与外部直流电源箱连接时不会出现接线错误,克服了传统技术中存在误将正负接反的问题。 In the present invention, the upper sealing cover 5 and the lower sealing cover 6 are metal titanium cover plates, and the opposite surface of the upper sealing cover 5 and the lower sealing cover 6 is coated with a layer of metal oxide coating with electrocatalytic activity, and the upper The sealing cover 5 and the lower sealing cover 6 correspond to the positive and negative electrodes of the external DC power supply respectively, so that the upper and lower sealing covers 6 and 6 are used as anodes regardless of the characteristics of titanium metal and the conductive properties of the metal oxide coating. Or cathode use all have conductivity, then, when connecting external DC power supply, if upper sealing cover 5 connects external DC power positive pole, then lower sealing cover 6 then connects negative pole; If upper sealing cover 5 connects the negative pole of external DC power supply, then The lower sealing cover 6 is connected to the positive pole; so that when the photoelectrochemical electrolysis device of the present invention is connected to an external DC power supply box, there will be no wiring errors, which overcomes the problem of mistakenly connecting positive and negative in the traditional technology.

上述实施例和附图并非限定本发明的产品形态和式样,任何所属技术领域的普通技术人员对其所做的适当变化或修饰,皆应视为不脱离本发明的专利范畴。 The above-mentioned embodiments and drawings do not limit the form and style of the product of the present invention, and any appropriate changes or modifications made by those skilled in the art should be considered as not departing from the patent scope of the present invention.

Claims (14)

1. a photoelectrochemistry electrolyzer, comprise electrolyzer and be located at silica tube, ultraviolet lamp and the battery lead plate in electrolyzer, this ultraviolet lamp is erected in this silica tube, this electrolyzer is provided with wastewater inlet and process water out; It is characterized in that: above-mentioned battery lead plate is provided with some, each battery lead plate keeps flat setting, and in being from top to bottom spaced, each battery lead plate has anode portion and the negative pole part of double setting, the first half portion faces of above-mentioned battery lead plate are coated with the coating of metal oxides with electro catalytic activity, the first half positions of this battery lead plate are above-mentioned anode portion, the surface-coated at the second half positions of above-mentioned battery lead plate has the semiconductor light-catalyst coating with photocatalytic activity, and the second half positions of above-mentioned battery lead plate are above-mentioned negative pole part;
The anode portion being in the battery lead plate of top in two battery lead plates setting up and down is be oppositely arranged up and down with the negative pole part of the battery lead plate being in below, insulating spacer is provided with between two battery lead plates, and each battery lead plate is serially connected by insulating support rod, above-mentioned silica tube is erect through each above-mentioned battery lead plate, and overlap wringing fit with above-mentioned battery lead plate, and the end, upper end of above-mentioned silica tube upwards passes outside above-mentioned electrolyzer.
2. photoelectrochemistry electrolyzer as claimed in claim 1, it is characterized in that: above-mentioned silica tube is provided with several, above-mentioned ultraviolet lamp is correspondingly provided with several, and with the corresponding setting one by one of above-mentioned silica tube, each above-mentioned ultraviolet lamp is connected with extraneous power electric by wire.
3. photoelectrochemistry electrolyzer as claimed in claim 1, is characterized in that: above-mentioned battery lead plate is mesh plate.
4. photoelectrochemistry electrolyzer as claimed in claim 1, is characterized in that: above-mentioned battery lead plate is metallic titanium plate, and above-mentioned coating of metal oxides is for containing RuO 2complex metal oxides coating or containing IrO 2multinary oxide coating layer, above-mentioned semiconductor light-catalyst coating is Cu 2o, ZnO, SnO 2, TiO 2in a kind of oxide coating, or above-mentioned semiconductor light-catalyst coating is Cu 2o, ZnO, SnO 2, TiO 2in two or more oxide compound composition compound coating.
5. photoelectrochemistry electrolyzer as claimed in claim 4, is characterized in that: above-mentioned complex metal oxides coating is RuO 2-TiO 2complex metal oxides coating, RuO 2-TiO 2-SnO 2complex metal oxides coating, RuO 2-SnO 2complex metal oxides coating, RuO 2-Ta 2o 5one in composite oxide coating; Above-mentioned multinary oxide coating layer is IrO 2-TiO 2binary oxide coating, IrO 2-TiO 2-SnO 2ternary oxide coating, IrO 2-SnO 2binary oxide coating, IrO 2-Ta 2o 2one in binary oxide coating.
6. photoelectrochemistry electrolyzer as claimed in claim 1, it is characterized in that: above-mentioned electrolyzer is square structure, above-mentioned electrolyzer is its upper and lower two ends is the hollow structure of open state, the upper end end face locking of above-mentioned electrolyzer has the top cover labyrinth of sealed electrolytic cell upper end open, above-mentioned top cover labyrinth has the rising pipe communicated with the hollow chamber of electrolyzer, the end, upper end of above-mentioned silica tube closely passes outside top cover labyrinth; The lower end surface locking of above-mentioned electrolyzer has the lower sealing cover of sealed electrolytic cell lower ending opening, above-mentioned lower sealing cover has the water inlet pipe communicated with the hollow chamber of electrolyzer.
7. photoelectrochemistry electrolyzer as claimed in claim 6, it is characterized in that: above-mentioned top cover labyrinth and lower sealing cover are metal titanium cover plate, the opposite face that above-mentioned top cover labyrinth is relative with above-mentioned lower sealing cover is coated with the coating of metal oxides that one deck has electro catalytic activity, and above-mentioned top cover labyrinth and lower sealing cover are corresponding to be respectively electrically connected with the positive and negative electrode of external dc power.
8. photoelectrochemistry electrolyzer as claimed in claim 6, it is characterized in that: sealed by the seal cartridge be sleeved on outside silica tube between above-mentioned silica tube and above-mentioned top cover labyrinth, above-mentioned top cover labyrinth offers the open holes passed for seal cartridge, above-mentioned seal cartridge is flush-mounted in above-mentioned open holes, and the edge, hole that the outer side wall of seal cartridge is arranged with for open holes is closely inserted into interior installation groove.
9. photoelectrochemistry electrolyzer as claimed in claim 1, it is characterized in that: above-mentioned support distance piece is hollow columnar structures, respectively to being convexly equipped with the support ring being stacked at battery lead plate upper and lower surface outward on the upper/lower terminal end outer side wall of above-mentioned support distance piece.
10. the battery lead plate for photoelectrochemistry electrolyzer, comprise plate electrode body, it is characterized in that: above-mentioned plate electrode body has anode portion and the negative pole part of double setting, the first half portion faces of above-mentioned plate electrode body are coated with the coating of metal oxides with electro catalytic activity, the first half positions of this plate electrode body are above-mentioned anode portion, the surface-coated at the second half positions of above-mentioned plate electrode body has the semiconductor light-catalyst coating with photocatalytic activity, and the second half positions of above-mentioned plate electrode body are above-mentioned negative pole part.
11. battery lead plates for photoelectrochemistry electrolyzer according to claim 10, is characterized in that: above-mentioned plate electrode body is vesicular structure.
12. battery lead plates for photoelectrochemistry electrolyzer according to claim 11, is characterized in that: above-mentioned plate electrode body is mesh plate, above-mentioned mesh plate is provided with several circular perforations.
13. battery lead plates for photoelectrochemistry electrolyzer according to claim 10, is characterized in that: above-mentioned plate electrode body is metallic titanium plate, and above-mentioned coating of metal oxides is for containing RuO 2complex metal oxides coating or containing IrO 2multinary oxide coating layer, above-mentioned semiconductor light-catalyst coating is Cu 2o, ZnO, SnO 2, TiO 2in a kind of oxide coating, or above-mentioned semiconductor light-catalyst coating is Cu 2o, ZnO, SnO 2, TiO 2in two or more oxide compound composition compound coating.
14. battery lead plates for photoelectrochemistry electrolyzer according to claim 13, is characterized in that: above-mentioned complex metal oxides coating is RuO 2-TiO 2complex metal oxides coating, RuO 2-TiO 2-SnO 2complex metal oxides coating, RuO 2-SnO 2complex metal oxides coating, RuO 2-Ta 2o 5one in composite oxide coating; Above-mentioned multinary oxide coating layer is IrO 2-TiO 2binary oxide coating, IrO 2-TiO 2-SnO 2ternary oxide coating, IrO 2-SnO 2binary oxide coating, IrO 2-Ta 2o 2one in binary oxide coating.
CN201510652210.3A 2015-10-10 2015-10-10 Optical electro-chemistry electrolysis installation and the battery lead plate for the optical electro-chemistry electrolysis installation Expired - Fee Related CN105293644B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510652210.3A CN105293644B (en) 2015-10-10 2015-10-10 Optical electro-chemistry electrolysis installation and the battery lead plate for the optical electro-chemistry electrolysis installation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510652210.3A CN105293644B (en) 2015-10-10 2015-10-10 Optical electro-chemistry electrolysis installation and the battery lead plate for the optical electro-chemistry electrolysis installation

Publications (2)

Publication Number Publication Date
CN105293644A true CN105293644A (en) 2016-02-03
CN105293644B CN105293644B (en) 2017-09-26

Family

ID=55191588

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510652210.3A Expired - Fee Related CN105293644B (en) 2015-10-10 2015-10-10 Optical electro-chemistry electrolysis installation and the battery lead plate for the optical electro-chemistry electrolysis installation

Country Status (1)

Country Link
CN (1) CN105293644B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106277180A (en) * 2016-08-24 2017-01-04 哈尔滨工程大学 A kind of intensified by ultrasonic wave photoelectrocatalysis processes containing heavy metal and the device of persistent organic pollutant wastewater
CN106587280A (en) * 2016-11-11 2017-04-26 西安交通大学 Photoelectrochemical method and device for cooperatively treating organic waste liquid and heavy metal waste liquid and generating electricity
CN106865688A (en) * 2017-03-31 2017-06-20 武汉市镱泰智能环保科技有限公司 A kind of upper up-flow photoelectrocatalysioxidization oxidization device
CN111837968A (en) * 2020-08-03 2020-10-30 诸城市中裕机电设备有限公司 High-efficient deodorization heat recovery unit

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5779912A (en) * 1997-01-31 1998-07-14 Lynntech, Inc. Photocatalytic oxidation of organics using a porous titanium dioxide membrane and an efficient oxidant
US6136186A (en) * 1997-01-31 2000-10-24 Lynntech, Inc. Photocatalytic oxidation of organics using a porous titanium dioxide membrane and an efficient oxidant
CN1377728A (en) * 2002-01-16 2002-11-06 中山大学 Three phase three-diemsnional electrode photoelectric reactor
CN1562795A (en) * 2004-04-07 2005-01-12 太原理工大学 Photoelectrocatalysis and oxidation device for treating organic substance in water
CN1966421A (en) * 2006-10-08 2007-05-23 暨南大学 Photoelectrical chemical synergistic catalytic reaction waste water treatment method and device
CN102101708A (en) * 2011-01-12 2011-06-22 中国科学院生态环境研究中心 Method and device for treating cyanide-containing wastewater through photoelectrochemistry
CN204173966U (en) * 2014-09-28 2015-02-25 常州大学 Three dimensional electrode photo electrocatalysis reaction unit
CN205170459U (en) * 2015-10-10 2016-04-20 泉州师范学院 Optical electro -Chemistry electrolysis equipment and be used for this optical electro -Chemistry electrolysis equipment's plate electrode

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5779912A (en) * 1997-01-31 1998-07-14 Lynntech, Inc. Photocatalytic oxidation of organics using a porous titanium dioxide membrane and an efficient oxidant
US6136186A (en) * 1997-01-31 2000-10-24 Lynntech, Inc. Photocatalytic oxidation of organics using a porous titanium dioxide membrane and an efficient oxidant
CN1377728A (en) * 2002-01-16 2002-11-06 中山大学 Three phase three-diemsnional electrode photoelectric reactor
CN1562795A (en) * 2004-04-07 2005-01-12 太原理工大学 Photoelectrocatalysis and oxidation device for treating organic substance in water
CN1966421A (en) * 2006-10-08 2007-05-23 暨南大学 Photoelectrical chemical synergistic catalytic reaction waste water treatment method and device
CN102101708A (en) * 2011-01-12 2011-06-22 中国科学院生态环境研究中心 Method and device for treating cyanide-containing wastewater through photoelectrochemistry
CN204173966U (en) * 2014-09-28 2015-02-25 常州大学 Three dimensional electrode photo electrocatalysis reaction unit
CN205170459U (en) * 2015-10-10 2016-04-20 泉州师范学院 Optical electro -Chemistry electrolysis equipment and be used for this optical electro -Chemistry electrolysis equipment's plate electrode

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106277180A (en) * 2016-08-24 2017-01-04 哈尔滨工程大学 A kind of intensified by ultrasonic wave photoelectrocatalysis processes containing heavy metal and the device of persistent organic pollutant wastewater
CN106587280A (en) * 2016-11-11 2017-04-26 西安交通大学 Photoelectrochemical method and device for cooperatively treating organic waste liquid and heavy metal waste liquid and generating electricity
CN106587280B (en) * 2016-11-11 2020-02-07 西安交通大学 Photoelectrochemical method and device for cooperatively treating organic waste liquid and heavy metal waste liquid and generating electricity
CN106865688A (en) * 2017-03-31 2017-06-20 武汉市镱泰智能环保科技有限公司 A kind of upper up-flow photoelectrocatalysioxidization oxidization device
CN106865688B (en) * 2017-03-31 2023-02-03 武汉市镱泰智能环保科技有限公司 Upflow photoelectrocatalysis oxidation device
CN111837968A (en) * 2020-08-03 2020-10-30 诸城市中裕机电设备有限公司 High-efficient deodorization heat recovery unit

Also Published As

Publication number Publication date
CN105293644B (en) 2017-09-26

Similar Documents

Publication Publication Date Title
CN105236628B (en) Electrical enhanced photocatalysis degraded sewage device
CN101693560B (en) Integral solar energy photoelectricity water-treatment device
Xie et al. Degradation of bisphenol A in aqueous solution by H2O2-assisted photoelectrocatalytic oxidation
Zhang et al. Electrochemical degradation of refractory pollutants using TiO2 single crystals exposed by high-energy {001} facets
CN106277180A (en) A kind of intensified by ultrasonic wave photoelectrocatalysis processes containing heavy metal and the device of persistent organic pollutant wastewater
CN102603037A (en) Sunlight-assisted electro-catalysis organic wastewater treatment membrane reactor
CN1263686C (en) Photoelectrocatalysis and oxidation device for treating organic substance in water
CN201381244Y (en) Device for continuous photocatalytic oxidation treatment of wastewater
CN102658130B (en) Preparation method of Ru-Pd bimetal-supported TiO2 nanotube photocatalyst and application thereof
CN102092820A (en) Method and device for removing organic matters from water by using double-pool double-effect visible light in response to photo-electro-Fenton reaction
CN105293644B (en) Optical electro-chemistry electrolysis installation and the battery lead plate for the optical electro-chemistry electrolysis installation
Poonia et al. Photoelectrocatalytic systems for simultaneous energy recovery and wastewater treatment: a review
Zhang et al. Coupling effects between metal–organic framework derivatives and oxygen-deficient TiO 2 nanotubes: identified charge-transfer processes and photoelectric synergistic effect
CN201043148Y (en) Photocatalytic and electrocatalytic co-processing device for organic wastewater
Zha et al. Treatment of hazardous organic amine wastewater and simultaneous electricity generation using photocatalytic fuel cell based on TiO2/WO3 photoanode and Cu nanowires cathode
WO2017076282A1 (en) Electrolytic tank apparatus using oxygen reduction cathode
CN205170459U (en) Optical electro -Chemistry electrolysis equipment and be used for this optical electro -Chemistry electrolysis equipment's plate electrode
CN106395998A (en) Salt-containing wastewater resourceful treatment method
Zheng et al. Interaction between InP and SnO2 on TiO2 nanotubes for photoelectrocatalytic reduction of CO2
CN107176654A (en) A kind of utilization solar energy cooperates with the set composite of processing sewage with photoelectrocatalysis
Chen et al. In-situ synchronous photoelectrosynthesis of H2O2/HClO green disinfectant with a S-scheme heterojunction bifunctional In2S3/MnIn2S4 photoelectrocatalyst
Li et al. Facile fabrication of SnO2/TiO2 nanotube arrays for efficient degradation of pollutants
CN205170458U (en) Photoelectricity concerted catalysis degradation sewage device
CN204151114U (en) A kind of cloth water structure of SPE electrolyzer
Leng et al. Synergy of dual photoelectrodes for simultaneous antibiotic degradation and CO2 reduction by Z-scheme PEC system

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

Granted publication date: 20170926