CN101798126A - Method for treating industrial waste water by means of photoelectrocatalysis - Google Patents
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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- Water Treatment By Electricity Or Magnetism (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
本发明提供了一种采用光电催化化学氧化或还原的方法处理工业废水的方法,属于环境保护领域,即采用钛阳极氧化法制备的高度有序的钛基TiO2纳米管阵列薄膜为光阳极或光阴极,高纯石墨为对电极,在连接外电路并在光辐射下将工业废水的有机物或重金属离子降解为H2O和CO2、低价金属离子或金属单质。本发明的优点在于:采用的催化剂光阳极是以阳极氧化自组装的垂直于钛基底的高度有序阵列薄膜,不仅克服了以往粉体负载薄膜光阳极结合力差、容易脱落及催化效率逐步衰减的缺陷,而且通过对该阵列薄膜的掺杂改性可直接利用太阳光,是一项节能、高效、高选择性、清洁、低成本处理单一(染料如造纸厂、印染厂有机废水,或重金属离子如电镀厂含铬废水)或复合废水的先进技术。
The invention provides a method for treating industrial waste water by photoelectrocatalytic chemical oxidation or reduction, which belongs to the field of environmental protection, that is, a highly ordered titanium-based TiO2 nanotube array film prepared by a titanium anodic oxidation method is used as a photoanode or Photocathode, with high-purity graphite as the counter electrode, degrades the organic matter or heavy metal ions of industrial wastewater into H 2 O and CO 2 , low-priced metal ions or metal elements when connected to an external circuit and under light radiation. The advantage of the present invention is that the catalyst photoanode adopted is a highly ordered array film perpendicular to the titanium substrate that is self-assembled by anodic oxidation, which not only overcomes the poor bonding force of the photoanode of the powder-loaded film in the past, the easy falling off and the gradual attenuation of catalytic efficiency defects, and can directly use sunlight by doping and modifying the array film, which is an energy-saving, high-efficiency, high-selectivity, clean, low-cost treatment of a single (dyes such as paper mills, organic wastewater from printing and dyeing plants, or heavy metals) Advanced technology for ions such as electroplating plant chromium-containing wastewater) or composite wastewater.
Description
技术领域technical field
本发明属于环境保护与治理方面的工业废水处理领域。采用钛阳极氧化制备的高度有序TiO2纳米管阵列薄膜为光电极材料,高纯石墨或贱金属材料为对电极,在0~3V直流偏压作用并在太阳光或模拟太阳光辐射下,将染料或农药废水中的有机物在阳极彻底矿化为H2O和CO2,将重金属离子还原成低价离子或金属单质。该技术结合了电催化和光催化的优点,通过外电路对光生电子的快速输运及电场辅助光生空穴的阴极迁移,加速光生电子-空穴对的分离,降低其复合的可能,可显著提高催化效率,是一项节能、高效、高选择性、清洁、低成本处理单一(染料如造纸厂、印染厂、制药厂的有机废水等,或重金属离子如电镀厂含铬废水、冶金工厂含汞废水等)或复合废水的先进技术。The invention belongs to the field of industrial waste water treatment in terms of environmental protection and treatment. The highly ordered TiO2 nanotube array film prepared by titanium anodic oxidation is used as the photoelectrode material, and the high-purity graphite or base metal material is used as the counter electrode. Under the action of 0-3V DC bias and under the irradiation of sunlight or simulated sunlight, The organic matter in the dye or pesticide wastewater is completely mineralized into H 2 O and CO 2 at the anode, and the heavy metal ions are reduced to low-valent ions or metal elements. This technology combines the advantages of electrocatalysis and photocatalysis, through the rapid transport of photogenerated electrons by the external circuit and the cathode migration of photogenerated holes assisted by the electric field, the separation of photogenerated electron-hole pairs is accelerated, and the possibility of their recombination is reduced, which can significantly improve Catalytic efficiency is an energy-saving, high-efficiency, high-selectivity, clean, low-cost treatment of a single (dye such as organic wastewater from paper mills, printing and dyeing factories, pharmaceutical factories, etc., or heavy metal ions such as chromium-containing wastewater from electroplating plants, and mercury from metallurgical factories. wastewater, etc.) or advanced technologies for complex wastewater.
背景技术Background technique
TiO2的带隙能为3.2eV(锐钛矿型),相当于波长为387.5nm光子能量。当TiO2受到波长小于387.5nm的紫外光照射时,价带上的电子跃迁到导带上,从而产生光生电子(e-)—空穴(h+)对。所产生的h+分别与吸附在TiO2颗粒表面的O2和H2O分子氧化生成O2 -和·OH自由基。O2 -和·OH这两种活性物质具有极强的氧化能力,完成氧化分解反应,尤其是·OH基,具有高达501KJ/mol的能量,而有机分子中的C-C,C-H,N-C,C-O,O-H,N-H键的键能分别为347KJ.mol-1,414KJ.mol-1,305KJ.mol-1,351KJ.mol-1,464KJ.mol-1,388KJ.mol-1,比·OH基的能量低得多。因此,许多种气相有机污染物都可以通过光催化氧化过程快速分解,包括脂肪烃、醇、醛、酮、卤代烃、芳烃、硫醇及杂原子有机物、NOx、SOx等,美国环保局公布了九大类114种有机物被证实可以通过光催化氧化处理。利用光催化氧化的方法处理生活用水可避免常规氯化法或臭氧法处理产生的氯仿或溴酸根等致癌附产物,达到深度矿化的目的,更显示出光催化氧化处理的优越性。该方法尤其适合于无法或难以生物降解的有毒有机物质的处理。The bandgap energy of TiO2 is 3.2eV (anatase type), which is equivalent to photon energy with a wavelength of 387.5nm. When TiO 2 is irradiated by ultraviolet light with a wavelength less than 387.5nm, the electrons in the valence band transition to the conduction band, thereby generating photogenerated electron (e - )-hole (h + ) pairs. The generated h + oxidized with O 2 and H 2 O molecules adsorbed on the surface of TiO 2 particles to generate O 2 - and ·OH radicals, respectively. The two active substances, O 2 - and ·OH, have extremely strong oxidizing ability to complete the oxidative decomposition reaction, especially the ·OH group, which has an energy as high as 501KJ/mol, while CC, CH, NC, CO, The bond energies of OH and NH bonds are 347KJ.mol -1 , 414KJ.mol -1 , 305KJ.mol -1 , 351KJ.mol -1 , 464KJ.mol -1 , 388KJ.mol -1 . Much lower energy. Therefore, many kinds of gaseous organic pollutants can be rapidly decomposed by photocatalytic oxidation process, including aliphatic hydrocarbons, alcohols, aldehydes, ketones, halogenated hydrocarbons, aromatics, mercaptans and heteroatom organic compounds, NO x , SO x , etc., US Environmental Protection The Bureau announced that 114 organic substances in nine categories have been confirmed to be treated by photocatalytic oxidation. The use of photocatalytic oxidation to treat domestic water can avoid carcinogenic by-products such as chloroform or bromate produced by conventional chlorination or ozone treatment, achieve the purpose of deep mineralization, and show the superiority of photocatalytic oxidation treatment. This method is especially suitable for the treatment of toxic organic substances that cannot or are difficult to biodegrade.
光生电子具有很强的还原能力,水中的重金属离子可通过接受二氧化钛表面上的电子而被还原。例如Cr6+具有较强的致癌性,其毒性比Cr3+高出100倍。在Cr6+-TiO2体系中[29-32],光生电子被Ti4+捕获而生成Ti3+,Cr6+的光催化还原主要从Ti3+上得到电子间接还原为主;该法也可用于某些贵金属低浓度水溶液中有价金属的综合回收或光催化还原防腐,还可用于光催化氧化/还原协同体系同时去除水中重金属离子和有机污染物,如对含金属离子Cr,Ag,Au,Cd,Cu,Hg,Ni和Pt等以及有机物甲醇、甲酸、水杨酸、EDTA、苯酚和硝基苯等的废水的光催化氧化/还原处理。Photogenerated electrons have a strong reducing ability, and heavy metal ions in water can be reduced by accepting electrons on the surface of titanium dioxide. For example, Cr 6+ is highly carcinogenic, and its toxicity is 100 times higher than that of Cr 3+ . In the Cr 6+ -TiO 2 system [29-32] , photogenerated electrons are captured by Ti 4+ to generate Ti 3+ , and the photocatalytic reduction of Cr 6+ is mainly indirect reduction of electrons obtained from Ti 3+ ; this method It can also be used for comprehensive recovery of valuable metals in low-concentration aqueous solutions of some precious metals or photocatalytic reduction for anticorrosion. It can also be used for photocatalytic oxidation/reduction synergistic systems to simultaneously remove heavy metal ions and organic pollutants in water, such as Cr and Ag containing metal ions. , Au, Cd, Cu, Hg, Ni and Pt, etc., as well as organic matter methanol, formic acid, salicylic acid, EDTA, phenol and nitrobenzene, etc. for photocatalytic oxidation/reduction treatment of wastewater.
早在1976年,日本学者Carey等就进行了TiO2光催化降解水中各类有机物的研究,在光照条件下以TiO2为催化剂可无选择性地氧化并彻底矿化多种有机物;次年Frank等研究了多种光催化剂,如TiO2、ZnO、CdS、WO3、Fe2O3在氙灯照射下污染物包括CN-、SO3 2-等的光催化降解,其反应速度均大于3.1×10-6mol.d-1.cm-2。由于二氧化钛无毒、低廉的成本、优异的耐酸碱和光化学腐蚀等特点,因此,近三十多年来关于TiO2光催化降解水中污染物一直是环境治理的热点课题,其研究的重点主要是通过掺杂、表面沉积、复合半导体等改性技术来调节TiO2的能带结构,从而使其光响应波长拓展到可见光区域,以利用清洁的太阳光并提高量子产率。然而,绝大多数研究都是采用超细或纳米TiO2粉体作光催化剂,这使催化剂的分离回收和循环利用相当困难,不可能得到广泛的工业应用。因此,近年来的研究转向纳米TiO2粉体固载,玻璃、陶瓷、金属、树脂、分子筛、活性碳、硅胶或多孔材料等都曾经被作为纳米TiO2粉体载体材料被研究过。但是,这种固载型催化剂在使用一段时间后会发生粉体脱落,随着使用时间的延长,其光催化效果呈逐渐衰减的趋势。直到1999年,Zwilling等在HF水溶液电解质中以高纯钛片为阳极、铂片为对电极,采用阳极氧化的方法制备了取向垂直于钛基体的高度有序的TiO2纳米管阵列薄膜,这种有序多孔结构材料既是载体,又是催化剂,解决了粉体负载后结合力差以及粉体催化剂难以回收循环利用的问题。与粉体光催化剂相比,TiO2纳米管阵列具有更大的比表面积,而且其高度有序垂直于表面的排列为光生电子在其中的传输提供了快捷的路径,可有效降低光生载流子在捕获、分离、传递等过程中的复合,从而显著提高光催化过程的量子产率,为光催化技术用于环境治理带来了新的希望。这一时期的研究工作主要围绕形成机制、形貌控制及改性处理以拓展光响应波长至可见光区域等课题,在这方面国内外很多学者开展了卓有成效的研究工作。目前,通过电化学条件的裁剪,完全能有效控制TiO2纳米管阵列的管长、管径及分布、壁厚等参数,制备出用于光电催化处理废水的钛基TiO2纳米管阵列材料,以此为光电催化处理废水的光电极材料,用于工业废水中有机或无机及其复合废水的处理。As early as 1976, Japanese scholar Carey et al. carried out research on TiO 2 photocatalytic degradation of various organic substances in water. Under light conditions, TiO 2 was used as a catalyst to non-selectively oxidize and completely mineralize various organic substances; the following year Frank studied the photocatalytic degradation of various photocatalysts, such as TiO 2 , ZnO, CdS, WO 3 , Fe 2 O 3 , pollutants including CN - , SO 3 2-, etc. 10 -6 mol.d -1 .cm -2 . Due to the non-toxicity, low cost, and excellent acid and alkali resistance and photochemical corrosion of titanium dioxide, the photocatalytic degradation of pollutants in water by TiO2 has been a hot topic in environmental governance for more than 30 years. The focus of its research is mainly The energy band structure of TiO 2 is adjusted by modification techniques such as doping, surface deposition, and compound semiconductor, so that its photoresponse wavelength is extended to the visible light region, so as to utilize clean sunlight and increase the quantum yield. However, most researches use ultrafine or nanometer TiO 2 powder as photocatalyst, which makes the separation, recovery and recycling of the catalyst quite difficult, and it is impossible to obtain a wide range of industrial applications. Therefore, research in recent years has turned to nano-TiO 2 powder immobilization, and glass, ceramics, metals, resins, molecular sieves, activated carbon, silica gel or porous materials have all been studied as nano-TiO 2 powder carrier materials. However, the powder of this solid-supported catalyst will fall off after being used for a period of time, and its photocatalytic effect will gradually decline with the prolongation of the use time. Until 1999, Zwilling et al. used a high-purity titanium sheet as an anode and a platinum sheet as a counter electrode in an HF aqueous electrolyte, and used an anodic oxidation method to prepare a highly ordered TiO 2 nanotube array film with an orientation perpendicular to the titanium matrix. The ordered porous structure material is not only a carrier, but also a catalyst, which solves the problems of poor binding force after the powder is loaded and difficult recovery and recycling of the powder catalyst. Compared with powder photocatalysts, the TiO2 nanotube array has a larger specific surface area, and its highly ordered arrangement perpendicular to the surface provides a fast path for the transmission of photogenerated electrons, which can effectively reduce the photogenerated charge carrier. The recombination in the processes of capture, separation, transfer, etc., thus significantly improving the quantum yield of the photocatalytic process, has brought new hope for the application of photocatalytic technology in environmental governance. The research work during this period mainly focused on the formation mechanism, morphology control and modification treatment to expand the photoresponse wavelength to the visible light region. Many scholars at home and abroad have carried out fruitful research work in this regard. At present, through the tailoring of electrochemical conditions, the parameters of the tube length, tube diameter, distribution, and wall thickness of the TiO 2 nanotube array can be effectively controlled, and titanium-based TiO 2 nanotube array materials for photoelectrocatalytic treatment of wastewater can be prepared. It is used as a photoelectrode material for photoelectric catalytic treatment of wastewater, and it is used for the treatment of organic or inorganic and their composite wastewater in industrial wastewater.
发明内容Contents of the invention
本发明的目的在于提供一种光电催化处理工业废水中有机或无机污染物的方法,该法结合了光催化和店催化的优点,以高度有序垂直于钛基底的二氧化钛纳米管阵列为光电极,并可直接利用清洁廉价的太阳光将其分解为无害物,适合于染料、制药、电镀及冶金工厂重金属离子废水的处理,是一种流程简短、清洁高效、操作简便的处理中低浓度工业废水的先进技术。The object of the present invention is to provide a method for photoelectrocatalytic treatment of organic or inorganic pollutants in industrial wastewater, which combines the advantages of photocatalysis and catalysis, and uses highly ordered titanium dioxide nanotube arrays perpendicular to the titanium substrate as photoelectrodes , and can directly use clean and cheap sunlight to decompose it into harmless substances. It is suitable for the treatment of heavy metal ion wastewater in dyestuffs, pharmaceuticals, electroplating and metallurgical factories. Advanced technology for industrial wastewater.
本发明采用光电催化方法处理工业废水中有机或无机污染物,具体的工艺为:(1)用阳极氧化的方法制备高度有序垂直于钛基底的二氧化钛纳米管阵列。以工业纯钛片(>99%)为起始材料,依次经过机械打磨、化学抛光、超声清洗处理,以其为阳极,石墨、镍片、铂或镀铂片为阴极,含氟的无机水溶液或有机溶液如C3H8O3、(CH3)2CHOH为电解质溶液,所采用的含氟溶液的浓度如HF、NH4F、NaF或KF为0.2~1.0wt%,阳极氧化过程的电压为20~60V,温度为5~20℃,时间为0.5~6h,阳极氧化后得到的二氧化钛薄膜为无定型,经在空气气氛下500℃,2h的晶化热处理使其转化为纯锐钛矿相;(2)将(1)所制备的锐钛矿型有序二氧化钛纳米管阵列为光电极,石墨或铁或贱金属为对电极,模拟太阳光(350W Xe灯)为光源,偏压为0~3V,将工业废水中有机或无机污染物光电催化降解为无害物质,如将其中有机物彻底分解为H2O和CO2,将高价的重金属离子还原为低价态或金属单质。The invention adopts a photoelectric catalysis method to treat organic or inorganic pollutants in industrial waste water, and the specific process is as follows: (1) preparing highly ordered titanium dioxide nanotube arrays perpendicular to the titanium substrate by an anodic oxidation method. The industrial pure titanium sheet (>99%) is used as the starting material, followed by mechanical grinding, chemical polishing, and ultrasonic cleaning, with it as the anode, graphite, nickel sheet, platinum or platinum-plated sheet as the cathode, and an inorganic aqueous solution containing fluorine Or an organic solution such as C 3 H 8 O 3 , (CH 3 ) 2 CHOH is the electrolyte solution, and the concentration of the fluorine-containing solution used, such as HF, NH 4 F, NaF or KF, is 0.2 to 1.0 wt%. The voltage is 20-60V, the temperature is 5-20°C, and the time is 0.5-6h. The titanium dioxide film obtained after anodic oxidation is amorphous, and it is transformed into pure anatase after crystallization heat treatment at 500°C for 2h in an air atmosphere. Mineral phase; (2) The anatase-type ordered titanium dioxide nanotube array prepared in (1) is used as a photoelectrode, graphite or iron or base metal is used as a counter electrode, simulated sunlight (350W Xe lamp) is used as a light source, and the bias voltage is 0~3V, photocatalytically degrades organic or inorganic pollutants in industrial wastewater into harmless substances, such as completely decomposing organic matter into H 2 O and CO 2 , and reducing high-priced heavy metal ions to low-valent states or metal elements.
本发明具有如下主要优点:(1)光电催化采用高度有序的TiO2纳米管阵列薄膜为光阳极材料,它充当了载体和催化剂的双重功能,解决了以往悬浮催化剂体系难以回收循环利用和固载型纳米TiO2粉体容易脱落的问题,而且其有序结构、较大的比表面积不仅为光电催化提供了更多的活性反应中心,而且还为光生电子和空穴的传递提供了快捷的通道,并借助外电场加速其分离过程,可有效地避免光生电子-空穴对的复合,提高催化活性;(2)通过掺杂改性处理完全可实现可见光响应和高选择性,从而可以直接利用太阳光进行废水的光电催化处理;(3)与常规的物理化学或生物化学方法相比,流程简短,且不产生二次污染物或形成污染物的物理转移;(4)反应条件温和、工艺对环境友好、操作和控制极其简便,其连续处理工艺可望用于量大、成分变化大且复杂、难以生化处理的废水处理,实现低成本、高效率、节能环保的工艺目标。据了解,目前处理染料废水的成本通常大于10元/米3,若用光电催化的方法处理成本将下降到4元/米3左右(对中低浓度废水),在阳光充足的地区如利用太阳光光催化,成本还可能进一步降低。The present invention has the following main advantages: (1) The highly ordered TiO2 nanotube array thin film is used as the photoanode material in photoelectrocatalysis, which serves as the dual function of carrier and catalyst, and solves the difficulty of recycling and solidification of the suspension catalyst system in the past. Supported nano-TiO 2 powder is easy to fall off, and its ordered structure and large specific surface area not only provide more active reaction centers for photocatalysis, but also provide a fast way for the transfer of photogenerated electrons and holes. channels, and the separation process is accelerated with the help of an external electric field, which can effectively avoid the recombination of photogenerated electron-hole pairs and improve the catalytic activity; Photocatalytic treatment of wastewater using sunlight; (3) Compared with conventional physical chemical or biochemical methods, the process is short and does not produce secondary pollutants or form physical transfer of pollutants; (4) The reaction conditions are mild, The process is environmentally friendly, and the operation and control are extremely simple. Its continuous treatment process is expected to be used for the treatment of wastewater with large volume, large composition changes and complexity, and difficult biochemical treatment, so as to achieve the process goals of low cost, high efficiency, energy saving and environmental protection. It is understood that the current cost of treating dye wastewater is usually more than 10 yuan/ m3 , and the cost will drop to about 4 yuan/m3 (for low- and medium-concentration wastewater) by using photoelectric catalysis. With photocatalysis, the cost may be further reduced.
XRD分析表明,本方法所制备的TiO2纳米管阵列为锐钛型。FE-SEM分析表明,用含氟水溶液电解质溶液所制备的二氧化钛纳米管阵列高度有序且垂直于钛基底排列,管长为300~800nm,管内径为100~300nm,壁厚为20~40nm;用含氟有机电解质溶液所制备的TiO2纳米管阵列同样垂直于钛基底生长,管长、管径、壁厚分别为0.8~20μm、80~150nm、15~25nm。在模拟太阳光(350WXe灯)照射下,光电催化氧化降解亚甲基蓝、氨氮废水或还原六价铬离子水溶液或降解含亚甲基蓝与六价铬离子的复合废水,本方法都具有很高的降解能力,在2~3小时内可将废水中的亚甲基蓝与六价铬离子完全降解。XRD analysis shows that the TiO 2 nanotube array prepared by this method is anatase. FE-SEM analysis shows that the titanium dioxide nanotube arrays prepared by the fluorine-containing aqueous electrolyte solution are highly ordered and arranged vertically to the titanium substrate, the tube length is 300-800nm, the tube inner diameter is 100-300nm, and the wall thickness is 20-40nm; The TiO 2 nanotube array prepared with fluorine-containing organic electrolyte solution also grows perpendicular to the titanium substrate, and the tube length, tube diameter, and wall thickness are 0.8-20 μm, 80-150 nm, and 15-25 nm, respectively. Under the irradiation of simulated sunlight (350WXe lamp), the photoelectric catalytic oxidation degradation of methylene blue, ammonia nitrogen wastewater or the reduction of hexavalent chromium ion aqueous solution or the degradation of composite wastewater containing methylene blue and hexavalent chromium ions, this method has a high degradation ability. The methylene blue and hexavalent chromium ions in the wastewater can be completely degraded within 2 to 3 hours.
附图说明Description of drawings
图1光电催化氧化亚甲基蓝溶液结果(初始浓度10mg/L),(a)0V bias,(b)+1V biasFigure 1 Photocatalytic oxidation of methylene blue solution (initial concentration 10mg/L), (a) 0V bias, (b) +1V bias
图2光电催化还原六价铬离子溶液结果(初始浓度20mg/L),(a)0V bias,(b)+1V biasFigure 2 Photocatalytic reduction of hexavalent chromium ion solution results (initial concentration 20mg/L), (a) 0V bias, (b) +1V bias
图3光电催化、吹脱、催化+吹脱处理氨氮废水的结果,(a)催化+吹脱,(b)吹脱,(c)光电催化Figure 3 The results of photoelectric catalysis, air stripping, catalysis + air stripping treatment of ammonia nitrogen wastewater, (a) catalysis + air stripping, (b) air stripping, (c) photoelectric catalysis
图4光电催化处理亚甲基蓝和六价铬离子的复合废水的试验结果,(a)六价铬离子降解;(b)亚甲基蓝降解Figure 4 Photocatalytic treatment of composite wastewater of methylene blue and hexavalent chromium ions, (a) degradation of hexavalent chromium ions; (b) degradation of methylene blue
图5本方法所制备的TiO2纳米管阵列的XRD图片,(a)热处理前(b)500℃,2h热处理后Figure 5 XRD pictures of TiO2 nanotube arrays prepared by this method, (a) before heat treatment (b) 500 ° C, after 2h heat treatment
图6本方法中用含氟水溶液电解质溶液植被的TiO2纳米管阵列的FE-SEM照片Fig. 6 FE-SEM photo of TiO2 nanotube arrays vegetated with fluorine-containing aqueous electrolyte solution in this method
图7本方法中用含氟有机溶液电解质溶液植被的TiO2纳米管阵列的FE-SEM照片Fig. 7 FE-SEM photo of TiO2 nanotube arrays vegetated with fluorine-containing organic solution electrolyte solution in this method
具体实施方式Detailed ways
实例1:Example 1:
以纯钛片(99.6%)为起始材料,依次经机械打磨、化学抛光、超声清洗后为阳极,高纯石墨片为阴极,0.5wt%HF水溶液为电解质,恒压氧化条件为:20V,30min,10±2℃;热处理条件:500℃,120min。用此条件下制备的TiO2纳米管阵列为光电极,高纯石墨为对电极,还是对六价铬离子,用本发明方法在3小时左右都能将其完全降解。Using pure titanium sheet (99.6%) as the starting material, it is mechanically polished, chemically polished, and ultrasonically cleaned in sequence as the anode, high-purity graphite sheet as the cathode, and 0.5wt% HF aqueous solution as the electrolyte. The constant pressure oxidation condition is: 20V, 30min , 10±2°C; heat treatment conditions: 500°C, 120min. The TiO nanotube array prepared under this condition is used as a photoelectrode, and the high-purity graphite is used as a counter electrode, or hexavalent chromium ions, which can be completely degraded in about 3 hours by the method of the present invention.
实例2:Example 2:
以纯钛片(99.6%)为起始材料,依次经机械打磨、化学抛光、超声清洗后为阳极,高纯石墨片为阴极,0.2wt%HF+0.3wt%NH4F+C3H8O3有机溶液为电解质,恒压氧化条件为:50V,6h,10±2℃;热处理条件:500℃,120min。用此条件下制备的TiO2纳米管阵列为光电极,高纯石墨为对电极,添加0.05M的Na2SO4,光电催化处理氨氮废水的结果见图3,试验条件:偏压+1.0V,温度30±5℃,空气流量250ml/min(对200毫升溶液),N起始浓度100mg/L,pH=11(用10%NaOH溶液调节)。从图3看,在光电催化同时吹脱的条件下,对于极难处理的氨氮废水,本发明方法也有极强的降解能力,3小时的降解率可达95%以上。Using pure titanium sheet (99.6%) as the starting material, after mechanical grinding, chemical polishing, and ultrasonic cleaning, the anode is used as the anode, and the high-purity graphite sheet is used as the cathode. 0.2wt% HF + 0.3wt% NH 4 F + C 3 H 8 O 3 The organic solution is the electrolyte, and the constant pressure oxidation condition is: 50V, 6h, 10±2°C; the heat treatment condition: 500°C, 120min. Using the TiO 2 nanotube array prepared under this condition as a photoelectrode, high-purity graphite as a counter electrode, and adding 0.05M Na 2 SO 4 , the results of photoelectric catalytic treatment of ammonia nitrogen wastewater are shown in Figure 3. Test conditions: bias +1.0V ,
实例3:Example 3:
以纯钛片(99.6%)为起始材料,依次经机械打磨、化学抛光、超声清洗后为阳极,高纯石墨片为阴极,0.2wt%HF+0.3wt%NH4F+C3H8O3有机溶液为电解质,恒压氧化条件为:50V,6h,10±2℃;热处理条件:500℃,120min。用此条件下制备的TiO2纳米管阵列为光电极,高纯石墨为对电极,光电催化处理亚甲基蓝和六价铬离子的复合废水的试验结果见图4。显然,对于六价铬离子,用本发明方法在40min左右能将其完全降解。对于亚甲基蓝,2h降解率可达76.49%。Using pure titanium sheet (99.6%) as the starting material, after mechanical grinding, chemical polishing, and ultrasonic cleaning, the anode is used as the anode, and the high-purity graphite sheet is used as the cathode. 0.2wt% HF + 0.3wt% NH 4 F + C 3 H 8 O 3 The organic solution is the electrolyte, and the constant pressure oxidation condition is: 50V, 6h, 10±2°C; the heat treatment condition: 500°C, 120min. Using the TiO2 nanotube array prepared under this condition as the photoelectrode, and the high-purity graphite as the counter electrode, the experimental results of the photoelectrocatalytic treatment of the composite wastewater of methylene blue and hexavalent chromium ions are shown in Figure 4. Obviously, for the hexavalent chromium ion, it can be completely degraded in about 40 minutes by the method of the present invention. For methylene blue, the 2h degradation rate can reach 76.49%.
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1598075A (en) * | 2004-07-29 | 2005-03-23 | 大连理工大学 | Titanium dioxide nano tube electrode and its preparation process and application |
CN101425396A (en) * | 2008-12-18 | 2009-05-06 | 浙江大学 | Boron doped titanic oxide nano tube thin-film photoelectric electrode and preparing method thereof |
CN101519233A (en) * | 2009-03-26 | 2009-09-02 | 上海交通大学 | Method for degrading organic substances by using photoelectric catalysis of short TiO2 nano-tube array film electrode |
-
2010
- 2010-04-23 CN CN201010157248A patent/CN101798126A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1598075A (en) * | 2004-07-29 | 2005-03-23 | 大连理工大学 | Titanium dioxide nano tube electrode and its preparation process and application |
CN101425396A (en) * | 2008-12-18 | 2009-05-06 | 浙江大学 | Boron doped titanic oxide nano tube thin-film photoelectric electrode and preparing method thereof |
CN101519233A (en) * | 2009-03-26 | 2009-09-02 | 上海交通大学 | Method for degrading organic substances by using photoelectric catalysis of short TiO2 nano-tube array film electrode |
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