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CN102001724B - Circulating water treatment device and process using nanocrystalline titanium dioxide fiber photocatalysis reactor - Google Patents

Circulating water treatment device and process using nanocrystalline titanium dioxide fiber photocatalysis reactor Download PDF

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CN102001724B
CN102001724B CN2010105030626A CN201010503062A CN102001724B CN 102001724 B CN102001724 B CN 102001724B CN 2010105030626 A CN2010105030626 A CN 2010105030626A CN 201010503062 A CN201010503062 A CN 201010503062A CN 102001724 B CN102001724 B CN 102001724B
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inner cylinder
titanium dioxide
quartz tube
nanocrystalline titanium
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CN102001724A (en
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刘和义
裴石光
刘金强
刘贵双
万青
陈炎
沈蕾
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Nanjing University of Science and Technology
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Abstract

本发明公开了一种用于有机污染物废水处理的利用纳米晶二氧化钛纤维光催化反应器组成的循环水处理装置及工艺。本发明在反应器的结构设计方面与现有技术相比有创新且优势明显:通过独特的进水扩径减速、均匀布流和内筒上口周圈溢流出水结构设计,在保证较大过水流量的同时,避免了水流流速过快导致纤维断碎流失;紫外灯置于反应器轴心位置,最大限度地利用了紫外光;充分考虑了在光催化反应进行的同时,对处理废水进行喷淋充氧;本发明结构简单,装配方便,造价低;所组成的光催化循环水处理工艺效率高、能耗低,可进行较大流量的连续化水处理,具有重要的实用价值。

Figure 201010503062

The invention discloses a circulating water treatment device and process for treating organic pollutant waste water, which is composed of a nanocrystalline titanium dioxide fiber photocatalytic reactor. Compared with the prior art, the present invention has innovations and obvious advantages in the structural design of the reactor: through the unique structure design of water inlet diameter expansion and deceleration, uniform flow distribution and overflow water outlet around the upper mouth of the inner cylinder, it can ensure a large While passing the water flow, it avoids the breakage and loss of fibers caused by too fast water flow rate; the ultraviolet lamp is placed at the axis of the reactor to maximize the use of ultraviolet light; fully consider the photocatalytic reaction while the waste water is treated Spray oxygenation; the invention has simple structure, convenient assembly and low cost; the formed photocatalytic circulating water treatment process has high efficiency and low energy consumption, and can carry out continuous water treatment with a relatively large flow rate, which has important practical value.

Figure 201010503062

Description

利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置及工艺Circulating water treatment device and process using nanocrystalline titanium dioxide fiber photocatalytic reactor

技术领域 technical field

本发明属于环保技术领域,特别是一种利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置及工艺。  The invention belongs to the technical field of environmental protection, in particular to a circulating water treatment device and process using a nanocrystalline titanium dioxide fiber photocatalytic reactor. the

背景技术 Background technique

半导体光催化氧化技术可以在紫外光照射下产生强氧化性自由基,快速无选择性地氧化分解水中各种有毒有机污染物,并可迅速杀灭水中的细菌和病毒,且不带来二次污染,操作简单,能耗低,在水处理领域应用前景十分广阔。  Semiconductor photocatalytic oxidation technology can generate strong oxidizing free radicals under ultraviolet light irradiation, quickly and non-selectively oxidize and decompose various toxic organic pollutants in water, and can quickly kill bacteria and viruses in water without causing secondary pollution. Pollution, simple operation, low energy consumption, very broad application prospects in the field of water treatment. the

在众多半导体光催化剂中,二氧化钛因光催化活性高、无毒无害,而备受关注。但二氧化钛的传统应用形态主要为纳米粉、薄膜和负载,均存在难以克服的缺陷,如纳米粉反应后与水分离回收困难,薄膜和负载比表面和活性低、易脱落,因此大大限制了其实际应用。纳米晶二氧化钛纤维的出现,则有望解决上述问题。由于其长径比极大的纤维形态优势,可以方便地设计填充式反应器,水可以直接流经纤维发生光催化反应,然后直接分离;同时,由于纤维本体即为二氧化钛纳米晶粒和纳米气孔共存的多晶体组织,比表面积大,光催化活性高,且在水中呈分散交织的三维分布状态,水和紫外光从间隙穿过反应,接触面积大,光催化效率高,因此有望实现高效连续的水处理工艺,具有重要的实际应用价值。专利CN.200410024265.1和CN.201010144227.5已发明了纳米晶二氧化钛纤维的制备方法,解决了材料的来源问题。  Among many semiconductor photocatalysts, titanium dioxide has attracted much attention due to its high photocatalytic activity, non-toxicity and harmlessness. However, the traditional application forms of titanium dioxide are mainly nano-powders, films and supports, all of which have insurmountable defects, such as the difficulty of separating and recycling nano-powders from water after reaction, and the low specific surface and activity of films and supports, which are easy to fall off, which greatly limits its use. practical application. The emergence of nanocrystalline titanium dioxide fibers is expected to solve the above problems. Due to the advantages of its fiber shape with a large aspect ratio, it is convenient to design a packed reactor, and water can flow directly through the fiber to undergo a photocatalytic reaction and then be separated directly; at the same time, because the fiber body is titanium dioxide nanocrystals and nanopores Coexisting polycrystalline structure, large specific surface area, high photocatalytic activity, and a three-dimensional distribution state of dispersion and interweaving in water, water and ultraviolet light pass through the gap to react, the contact area is large, and the photocatalytic efficiency is high, so it is expected to realize high-efficiency continuous The advanced water treatment process has important practical application value. Patents CN.200410024265.1 and CN.201010144227.5 have invented the preparation method of nanocrystalline titanium dioxide fiber, which solved the problem of the source of the material. the

要实现高效连续的纳米晶二氧化钛纤维光催化水处理,首先应进行纳米晶二氧化钛纤维光催化反应器的主体结构优化设计,其次要利用该反应器组成一套简便有效的水循环工艺。  In order to achieve efficient and continuous nanocrystalline titanium dioxide fiber photocatalytic water treatment, the main structure of the nanocrystalline titanium dioxide fiber photocatalytic reactor should be optimized first, and secondly, the reactor should be used to form a simple and effective water circulation process. the

进行纳米晶二氧化钛纤维光催化反应器的主体结构优化设计时,需重点考虑以下问题:①如何在保证较大处理水量的同时,降低水和纤维接触范围内的水流速度,避免因水流过急导致纤维断碎、流失;②如何最大限度地利用紫外光,降低光损耗,且实现光在反应器内均匀照射;③反应器应结构简单、制作装配方便、造价低。  When optimizing the main structure of the nanocrystalline titanium dioxide fiber photocatalytic reactor, the following issues need to be considered: ① How to reduce the water flow velocity in the contact range between water and fiber while ensuring a large amount of water to be treated, so as to avoid excessive water flow causing Fiber breakage and loss; ② How to maximize the use of ultraviolet light, reduce light loss, and achieve uniform irradiation of light in the reactor; ③ The reactor should be simple in structure, easy to manufacture and assemble, and low in cost. the

现有技术尚未能全部且很好地解决上述问题,如专利CN.200720021917.5、 CN.200720030678.x和CN.201010105477.8所公开的几种类型的二氧化钛纤维光催化反应装置,未充分考虑大流速水流冲击纤维的问题,特别是在出水口处,由于直接在反应器壁设出水口,导致水流截面积突然缩小,水流速在出水口处急剧加快,极易携带纤维流出水口;紫外光照射采用光纤传输太阳光紫外线,存在光传输损耗大、发光点不均匀、成本高的问题,或采用紫外灯源在反应器上方照射,光浪费较严重;反应器整体存在结构复杂、纤维装配不方便、造价高等问题。此外,光催化反应的进行还必须要有O2参与,而上述专利均未考虑这一问题。现有技术也尚未利用二氧化钛纤维光催化反应器组成一套完整的水处理工艺。  The prior art has not been able to completely and well solve the above problems, such as several types of titanium dioxide fiber photocatalytic reaction devices disclosed in patents CN. The problem of impacting fibers, especially at the water outlet, because the water outlet is directly set on the wall of the reactor, the cross-sectional area of the water flow is suddenly reduced, and the water flow speed is sharply accelerated at the water outlet, which is very easy to carry the fiber out of the water outlet; the ultraviolet light irradiation adopts optical fiber The transmission of ultraviolet rays from sunlight has the problems of large light transmission loss, uneven luminous points, and high cost, or the use of ultraviolet light sources to irradiate above the reactor, resulting in serious light waste; the overall structure of the reactor is complicated, fiber assembly is inconvenient, and the cost is high. advanced questions. In addition, O2 must be involved in the photocatalytic reaction, and none of the above-mentioned patents considers this issue. In the prior art, titanium dioxide fiber photocatalytic reactors have not yet been used to form a complete water treatment process.

发明内容 Contents of the invention

本发明针对现有技术缺陷,提供了一种结构合理、安装方便、造价低的纳米晶二氧化钛纤维光催化反应器,并利用该反应器组成一套完整的循环水处理装置及工艺,可进行较大流量的高效化、连续化循环水处理作业。  Aiming at the defects of the prior art, the present invention provides a nanocrystalline titanium dioxide fiber photocatalytic reactor with reasonable structure, convenient installation and low cost, and uses the reactor to form a complete set of circulating water treatment device and process, which can carry out comparative High-efficiency and continuous circulating water treatment operations with large flows. the

实现本发明目的的技术解决方案为:一种利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置由纳米晶二氧化钛纤维光催化反应器、储水池、水泵、第一阀门、流量计、第二阀门和喷淋曝气头构成水循环回路;其中,储水池出水口与水泵进水口相连,水泵出水口分为两路,其中一路与第一阀门连接,另一路与第二阀门相连,第一阀门与流量计进水口相连,流量计出水口与纳米晶二氧化钛纤维光催化反应器进水口相连,纳米晶二氧化钛纤维光催化反应器出水口通过管道通向储水池上方,第二阀门与喷淋曝气头相连,喷淋曝气头位于储水池上方。 纳米晶二氧化钛纤维光催化反应器包括外筒、内筒、石英管、紫外灯、纳米晶二氧化钛纤维、进水管口、多孔布流板、出水管口、有机纤维棉过滤层和石英管夹具;外筒、内筒和石英管由外而内呈同心圆布置;外筒和内筒竖向放置,两者上口均为通口,且外筒上口高度高于内筒上口高度,外筒下口高度也高于内筒下口高度,外筒下口设有一出水管口,外筒与内筒之间的环形间隙底部周圈封闭;进水管口呈直径逐渐扩大的圆锥形,并与内筒下口相连,交界处设有多孔布流板,多孔布流板上方铺设一层有机纤维棉过滤层-;沿内筒轴心方向设有石英管,石英管下口封闭,石英管最底部与有机纤维棉过滤层-接触,石英管上口为通口,石英管上口高度高于外筒上口高度;石英管内置有紫外灯;内筒和石英管之间填充纳米晶二氧化钛纤维,内筒上口出水位置再铺设一层有机纤维棉过滤层-。石英管通过夹具夹持定位,其中处于内筒下部和上部位置的第一夹具-和第二夹具-,分别夹持住石英管并使其固定于内筒的轴心方向,处于最顶端位置的第三夹具-夹持住石英管并与外筒的上口周圈用螺丝固定,以使石英管上下位置固定。  The technical solution to realize the object of the present invention is: a circulating water treatment device utilizing a nanocrystalline titanium dioxide fiber photocatalytic reactor consists of a nanocrystalline titanium dioxide fiber photocatalytic reactor, a water storage tank, a water pump, a first valve, a flow meter, a second The valve and the spray aerator head constitute a water circulation loop; among them, the water outlet of the storage tank is connected with the water inlet of the water pump, and the water outlet of the water pump is divided into two paths, one of which is connected with the first valve, and the other is connected with the second valve, and the first valve It is connected to the water inlet of the flowmeter, and the water outlet of the flowmeter is connected to the water inlet of the nanocrystalline titanium dioxide fiber photocatalytic reactor. The head is connected, and the spray aeration head is located above the water storage tank. Nanocrystalline titanium dioxide fiber photocatalytic reactor includes outer cylinder, inner cylinder, quartz tube, ultraviolet lamp, nanocrystalline titanium dioxide fiber, water inlet, porous distribution plate, water outlet, organic fiber cotton filter layer and quartz tube fixture; The cylinder, inner cylinder and quartz tube are arranged in concentric circles from the outside to the inside; the outer cylinder and the inner cylinder are placed vertically, and the upper openings of both are openings, and the height of the upper opening of the outer cylinder is higher than that of the inner cylinder. The height of the lower opening is also higher than that of the lower opening of the inner cylinder. The lower opening of the outer cylinder is provided with a water outlet pipe, and the bottom circumference of the annular gap between the outer cylinder and the inner cylinder is closed; The lower opening of the inner cylinder is connected, and a porous flow distribution plate is arranged at the junction, and a layer of organic fiber cotton filter layer is laid above the porous flow distribution plate; a quartz tube is arranged along the axial direction of the inner cylinder, and the lower opening of the quartz tube is closed. The bottom is in contact with the filter layer of organic fiber cotton, the upper opening of the quartz tube is a through opening, and the height of the upper opening of the quartz tube is higher than that of the upper opening of the outer cylinder; the quartz tube has a built-in ultraviolet lamp; the inner cylinder and the quartz tube are filled with nanocrystalline titanium dioxide fibers , and then lay a layer of organic fiber cotton filter layer at the water outlet position of the inner cylinder. The quartz tube is clamped and positioned by clamps, among which the first clamp - and the second clamp - at the lower and upper positions of the inner cylinder respectively clamp the quartz tube and fix it in the axial direction of the inner cylinder, and the one at the topmost position The third fixture-clamp the quartz tube and fix it with the upper circle of the outer cylinder with screws, so that the upper and lower positions of the quartz tube are fixed. the

具体的工艺流程如下:将含有机污染物的废水注入储水池内,开启水泵和紫外灯,废水则从储水池左端经水泵泵出,泵出的水分为左右两路,其中左路水经第一阀门调节流量后流经流量计,通过括径圆锥形进水管口流入纳米晶二氧化钛纤维光催化反应器的内筒,由于进水管口的直径逐渐扩大,水流横截面积相应扩大,水流速度显著降低,再经多孔布流板和有机纤维棉过滤层进一步均匀布流后,水流平稳缓慢上升,流经被紫外灯照射的纳米晶二氧化钛纤维的间隙,在纤维表面发生光催化反应,水中有机污染物得以降解和矿化,水流上升至内筒上方,经有机纤维棉过滤层过滤后,沿内筒的上口周圈溢流而下,流至内筒和外筒的间隙底部,经出水管口流出反应器,最后自流回储水池的右端;水泵泵出的右路水经第二阀门控制流量后,直接到达储水池右上方的喷淋曝气头,从喷淋曝气头的多个小孔射流喷出,进行曝气充氧,富含溶解氧的废水喷入储水池右端,再流向左端经水泵泵出,形成循环。  The specific process is as follows: inject the waste water containing organic pollutants into the storage tank, turn on the water pump and the ultraviolet lamp, and the waste water will be pumped out from the left end of the storage tank through the water pump. After the flow is adjusted by a valve, it flows through the flowmeter, and flows into the inner cylinder of the nanocrystalline titanium dioxide fiber photocatalytic reactor through the conical water inlet with a diameter. As the diameter of the water inlet gradually expands, the cross-sectional area of the water flow increases accordingly, and the water flow speed is significantly increased. After being lowered, and then distributed evenly through the porous flow plate and organic fiber cotton filter layer, the water flow rises steadily and slowly, and flows through the gaps of nanocrystalline titanium dioxide fibers irradiated by ultraviolet lamps, where photocatalytic reactions occur on the surface of the fibers, reducing organic pollution in water. The substances are degraded and mineralized, the water flow rises to the top of the inner cylinder, and after being filtered by the organic fiber cotton filter layer, it overflows along the upper circle of the inner cylinder, flows to the bottom of the gap between the inner cylinder and the outer cylinder, and passes through the outlet pipe. The outlet flows out of the reactor, and finally flows back to the right end of the storage tank by itself; the right water pumped out by the pump passes through the second valve to control the flow, and then directly reaches the spray aerator head on the upper right of the water storage tank. The small hole jet is sprayed out for aeration and oxygenation, and the wastewater rich in dissolved oxygen is sprayed into the right end of the storage tank, and then flows to the left end and is pumped out by the water pump to form a cycle. the

本发明与现有技术相比,其显著优点:  Compared with the prior art, the present invention has significant advantages:

(1)通过独特的进水扩径减速、均匀布流和内筒上口周圈溢流出水结构设计,在保证较大过水流量的同时,避免了水流流速过快导致纤维断碎流失。废水经括径圆锥形进水管口进入反应器内筒时,水流截面积扩大数十倍,使水流流速大大减缓,再经多孔布流板和有机纤维棉过滤层均匀布流,确保水流上升平稳缓慢,不会对二氧化钛纤维造成冲刷破坏作用;反应器的出水,不是直接在器壁开设出口,而是沿反应器内筒上口周圈溢流而出,大大增加了出水流通面积,并设有有机纤维棉过滤层过滤阻挡,确保纤维不会随出水流失。若直接在器壁开设出口,因水流截面积突然变小,管口流速急剧增加,会携带纤维流出反应器。  (1) Through the unique structural design of water inlet diameter expansion and deceleration, uniform flow distribution and overflow water outlet around the upper mouth of the inner cylinder, while ensuring a large water flow rate, it avoids fiber breakage and loss caused by too fast water flow. When the waste water enters the inner cylinder of the reactor through the conical inlet pipe with diameters, the cross-sectional area of the water flow is expanded dozens of times, which greatly slows down the flow rate of the water flow, and then the flow is evenly distributed through the porous flow distribution plate and the filter layer of organic fiber cotton to ensure the smooth rise of the water flow It is slow and will not cause scouring and damage to the titanium dioxide fibers; the outlet water of the reactor does not directly open an outlet on the wall of the reactor, but overflows along the upper circle of the inner cylinder of the reactor, which greatly increases the flow area of the outlet water and is designed There is an organic fiber cotton filter layer to filter and block to ensure that the fibers will not be lost with the water. If the outlet is directly opened on the wall of the vessel, the flow velocity at the orifice will increase sharply due to the sudden reduction of the cross-sectional area of the water flow, which will carry the fibers out of the reactor. the

(2)最大限度地利用了紫外光,几乎无光损耗。紫外灯置于反应器轴心位置,所发出的紫外光呈辐射状射出,可被外围的纳米晶二氧化钛纤维层层吸收,光照均匀,光利用率极高。  (2) Maximize the use of ultraviolet light, almost no light loss. The ultraviolet lamp is placed at the axis of the reactor, and the emitted ultraviolet light is radiated out, which can be absorbed by the surrounding nanocrystalline titanium dioxide fibers layer by layer, with uniform illumination and high light utilization efficiency. the

(3)充分考虑了在光催化反应进行的同时,对处理废水进行喷淋充氧。光催化氧化反应进行时,O2的参与极其重要,吸附于催化剂表面上的氧是光生电子e-的主要俘获剂,是e-的有效接受体,氧与e-的还原反应不仅生成表面光催化氧化反应所需的羟基自由基(·OH),而且为空穴提供所需的OH-和H2O,进一步生成·OH,形成一个良性的表面光催化过程,减少半导体光催化剂表面电子-空穴对的复合率,大大提高反应速率。  (3) It is fully considered that the photocatalytic reaction is carried out while spraying and oxygenating the treated wastewater. When the photocatalytic oxidation reaction proceeds, the participation of O 2 is extremely important. The oxygen adsorbed on the surface of the catalyst is the main capture agent of photogenerated electron e - and the effective acceptor of e - . The reduction reaction of oxygen and e - not only generates surface photocatalytic Hydroxyl radicals (·OH) required for the oxidation reaction, and provide the required OH - and H 2 O for holes, and further generate ·OH, forming a benign surface photocatalytic process, reducing the surface electron-holes of semiconductor photocatalysts The right recombination rate greatly increases the reaction rate.

本发明通过将水泵出水分为两路,其中一路进行喷淋曝气充氧,富含溶解氧的废水再来进行光催化反应,效率大大提高。  In the present invention, the pumped water is divided into two paths, one of which is sprayed, aerated and oxygenated, and the wastewater rich in dissolved oxygen is then subjected to photocatalytic reaction, so that the efficiency is greatly improved. the

(4)本发明的纳米晶二氧化钛纤维光催化反应器结构简单,装配方便,造价低。  (4) The nanocrystalline titanium dioxide fiber photocatalytic reactor of the present invention has simple structure, convenient assembly and low cost. the

(5)本发明的纳米晶二氧化钛纤维光催化循环水处理工艺光催化效率高、能耗低,可进行较大流量的连续化水处理,具有重要的实用价值。  (5) The nanocrystalline titanium dioxide fiber photocatalytic circulating water treatment process of the present invention has high photocatalytic efficiency and low energy consumption, and can carry out continuous water treatment with a large flow rate, and has important practical value. the

附图说明 Description of drawings

图1是本发明利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置与工艺的流程示意图。  Fig. 1 is a schematic flow diagram of a circulating water treatment device and process using a nanocrystalline titanium dioxide fiber photocatalytic reactor according to the present invention. the

图2是本发明纳米晶二氧化钛纤维光催化反应器横截面示意图。  Fig. 2 is a schematic cross-sectional view of the nanocrystalline titanium dioxide fiber photocatalytic reactor of the present invention. the

具体实施方式 Detailed ways

下面结合附图对本发明作进一步说明。  The present invention will be further described below in conjunction with accompanying drawing. the

结合图1,本发明利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置,由纳米晶二氧化钛纤维光催化反应器1、储水池2、水泵3、第一阀门4、流量计5、第二阀门6和喷淋曝气头7构成水循环回路;其中,储水池2出水口与水泵3进水口相连,水泵3出水口分为两路,其中一路与第一阀门4连接,另一路与第二阀门6相连,第一阀门4与流量计5进水口相连,流量计5出水口与纳米晶二氧化钛纤维光催化反应器1进水口相连,纳米晶二氧化钛纤维光催化反应器1出水口通过管道通向储水池2上方,第二阀门6与喷淋曝气头7相连,喷淋曝气头7位于储水池2上方。  In conjunction with Fig. 1, the present invention utilizes the circulating water treatment device of nanocrystalline titanium dioxide fiber photocatalytic reactor, consists of nanocrystalline titanium dioxide fiber photocatalytic reactor 1, water storage tank 2, water pump 3, first valve 4, flow meter 5, second The valve 6 and the spray aeration head 7 form a water circulation circuit; wherein, the water outlet of the water storage tank 2 is connected with the water inlet of the water pump 3, and the water outlet of the water pump 3 is divided into two routes, one of which is connected with the first valve 4, and the other is connected with the second valve 4. The valve 6 is connected, the first valve 4 is connected with the water inlet of the flow meter 5, the water outlet of the flow meter 5 is connected with the water inlet of the nanocrystalline titanium dioxide fiber photocatalytic reactor 1, and the water outlet of the nanocrystalline titanium dioxide fiber photocatalytic reactor 1 is connected to the Above the water storage tank 2, the second valve 6 is connected with the spray aeration head 7, and the spray aeration head 7 is located above the water storage tank 2. the

纳米晶二氧化钛纤维光催化反应器1由外筒10、内筒11、石英管12、紫外灯13、纳米晶二氧化钛纤维14、进水管口15、多孔布流板16、出水管口17、有机纤维棉过滤层18和石英管夹具19构成,其具体构造为:外筒10、内筒11 和石英管12由外而内呈同心圆布置;外筒10和内筒11均为直形圆筒,竖向放置,两者上口均为通口,且外筒10上口高度高于内筒11上口高度,外筒10下口高度也高于内筒11下口高度,外筒10下口设有一出水管口17,外筒10与内筒11之间的环形间隙底部周圈封闭;进水管口15呈直径逐渐扩大的圆锥形状,并与内筒[11]下口相连,交界处设有多孔布流板16,多孔布流板16为均匀布有1-3mm小孔的圆形平板,达到均匀分布水流的作用,多孔布流板16上方铺设一层有机纤维棉过滤层18-1,起到过滤进水和进一步均匀布流的作用;沿内筒轴心方向设有石英管12,石英管12下口封闭,石英管12最底部与有机纤维棉过滤层18-1接触,石英管12上口为通口,石英管12上口高度高于外筒10上口高度;石英管12内置有紫外灯13;内筒11和石英管12之间(从有机纤维棉过滤层18-1向上至接近内筒11上口之间的区域)填充纳米晶二氧化钛纤维14,内筒11上口出水位置(即纳米晶二氧化钛纤维14顶部)再铺设一层有机纤维棉过滤层18-2,起到过滤出水和阻挡纳米晶二氧化钛纤维随水流失的作用。  The nanocrystalline titanium dioxide fiber photocatalytic reactor 1 is composed of an outer cylinder 10, an inner cylinder 11, a quartz tube 12, an ultraviolet lamp 13, a nanocrystalline titanium dioxide fiber 14, a water inlet 15, a porous distribution plate 16, an outlet 17, organic fibers Cotton filter layer 18 and quartz tube clamp 19 constitute, and its specific structure is: outer tube 10, inner tube 11 and quartz tube 12 are arranged in concentric circles from outside to inside; Outer tube 10 and inner tube 11 are straight cylinders, Vertically placed, the upper openings of both are through openings, and the height of the upper opening of the outer cylinder 10 is higher than that of the upper opening of the inner cylinder 11, the height of the lower opening of the outer cylinder 10 is also higher than that of the lower opening of the inner cylinder 11, and the height of the lower opening of the outer cylinder 10 is higher than that of the inner cylinder 11. A water outlet pipe mouth 17 is provided, and the bottom circumference of the annular gap between the outer cylinder 10 and the inner cylinder 11 is closed; the water inlet pipe mouth 15 is in the shape of a cone whose diameter gradually expands, and is connected with the lower mouth of the inner cylinder [11]. There is a porous flow distribution plate 16, which is a circular flat plate evenly distributed with small holes of 1-3mm to achieve the effect of evenly distributing water flow, and a layer of organic fiber cotton filter layer 18-1 is laid on the top of the porous flow distribution plate 16 , play the role of filtering influent water and further evenly distributing the flow; a quartz tube 12 is arranged along the axial direction of the inner cylinder, the lower opening of the quartz tube 12 is closed, and the bottom of the quartz tube 12 is in contact with the organic fiber cotton filter layer 18-1, and the quartz tube 12 is in contact with the organic fiber cotton filter layer 18-1. The top of the tube 12 is a port, and the height of the top of the quartz tube 12 is higher than the height of the top of the outer cylinder 10; the quartz tube 12 is built with an ultraviolet lamp 13; 1 up to the area between the upper opening of the inner cylinder 11) to fill the nanocrystalline titanium dioxide fiber 14, and then lay a layer of organic fiber cotton filter layer 18-2 at the water outlet position of the upper opening of the inner cylinder 11 (i.e. the top of the nanocrystalline titanium dioxide fiber 14), Play the role of filtering out water and blocking the loss of nanocrystalline titanium dioxide fibers with water. the

本发明利用纳米晶二氧化钛纤维光催化反应器的循环水处理工艺,其具体工艺流程为:将含有机污染物的废水(预先经过过滤处理,不含固体悬浮物)注入储水池2内,开启水泵3和紫外灯13,废水则从储水池2左端经水泵3泵出,泵出的水分为左右两路,其中左路水经第一阀门4调节流量后流经流量计5,通过扩径圆锥形进水管口15流入纳米晶二氧化钛纤维光催化反应器1的内筒11,由于进水管口15的直径逐渐扩大,水流横截面积相应扩大,水流速度显著降低,再经多孔布流板16和有机纤维棉过滤层18-1进一步均匀布流后,水流平稳缓慢上升,流经被紫外灯13照射的纳米晶二氧化钛纤维14的间隙,在纤维表面发生光催化反应,水中有机污染物得以降解和矿化,水流上升至内筒11上方,经有机纤维棉过滤层18-2过滤后,沿内筒11的上口周圈溢流而下,流至内筒11和外筒10的间隙底部,经出水管口17流出反应器1,最后自流回储水池2的右端;水泵3泵出的右路水经第二阀门6控制流量后,直接到达储水池2右上方的喷淋曝气头7,从喷淋曝气头7的多个小孔射流喷出,进行曝气充氧,富含溶解氧的废水喷入储水池2右端,再流向左端经水泵3泵出,形成循环,循环一定时间后,废水中所含有机物可全部降解,直至彻底矿化为CO2和H2O。  The present invention utilizes the circulating water treatment process of the nanocrystalline titanium dioxide fiber photocatalytic reactor, and its specific process flow is: inject waste water containing organic pollutants (filtered in advance, without solid suspended matter) into the water storage tank 2, and turn on the water pump 3 and the ultraviolet lamp 13, the waste water is pumped out from the left end of the storage tank 2 through the water pump 3, and the pumped water is divided into left and right paths, wherein the water in the left path flows through the flow meter 5 after being adjusted by the first valve 4, and passes through the expanding cone Shaped water inlet pipe mouth 15 flows into the inner cylinder 11 of nanocrystalline titanium dioxide fiber photocatalytic reactor 1, because the diameter of water inlet pipe mouth 15 expands gradually, the water flow cross-sectional area expands correspondingly, and the water flow velocity significantly reduces, and then passes through porous flow distribution plate 16 and After the organic fiber cotton filter layer 18-1 is further evenly distributed, the water flow rises steadily and slowly, flows through the gaps of the nanocrystalline titanium dioxide fibers 14 irradiated by the ultraviolet lamp 13, and a photocatalytic reaction occurs on the surface of the fibers, and the organic pollutants in the water are degraded and eliminated. Mineralization, the water flow rises to the top of the inner cylinder 11, and after being filtered by the organic fiber cotton filter layer 18-2, it overflows along the upper circumference of the inner cylinder 11 and flows to the bottom of the gap between the inner cylinder 11 and the outer cylinder 10, It flows out of the reactor 1 through the outlet pipe 17, and finally flows back to the right end of the storage tank 2 by itself; the right-hand water pumped out by the water pump 3 is controlled by the second valve 6, and then directly reaches the spray aerator head 7 on the upper right of the storage tank 2 , sprayed from a plurality of small hole jets in the spray aerator head 7 to aerate and oxygenate, the wastewater rich in dissolved oxygen is sprayed into the right end of the storage tank 2, and then flows to the left end and is pumped out by the water pump 3 to form a cycle, which is constant After a period of time, the organic matter contained in the wastewater can be completely degraded until completely mineralized into CO 2 and H 2 O.

本发明原理如下:  Principle of the present invention is as follows:

本发明的工艺流程中,废水经括径圆锥形进水管口进入反应器内筒时,水流截面积扩大数十倍,使水流流速大大减缓,再经多孔布流板和有机纤维棉过滤层均匀布流,确保水流上升平稳缓慢,不会对二氧化钛纤维造成冲刷破坏作用;反应器的出水,不是直接在器壁开设出口,而是沿反应器内筒上口周圈溢流而出,大大增加了出水流通面积,并设有有机纤维棉过滤层过滤阻挡,确保纤维不会随出水流失。若直接在器壁开设出口,因水流截面积突然变小,管口流速急剧增加,会携带纤维流出反应器。  In the technological process of the present invention, when the waste water enters the inner cylinder of the reactor through the conical inlet pipe with diameters, the cross-sectional area of the water flow is enlarged dozens of times, so that the flow velocity of the water flow is greatly slowed down, and then the waste water passes through the porous distribution plate and the filter layer of organic fiber cotton. The flow distribution ensures that the water flow rises steadily and slowly, and will not cause scouring and damage to the titanium dioxide fibers; the water outlet of the reactor does not directly open an outlet on the wall, but overflows along the inner circle of the reactor inner cylinder, greatly increasing The water flow area is enlarged, and there is an organic fiber cotton filter layer to filter and block, so as to ensure that the fibers will not be lost with the water. If the outlet is directly opened on the wall of the vessel, the flow velocity at the orifice will increase sharply due to the sudden reduction of the cross-sectional area of the water flow, which will carry the fibers out of the reactor. the

本发明在充分考虑了在光催化反应进行的同时,对处理废水进行喷淋充氧。光催化氧化反应进行时,O2的参与极其重要,吸附于催化剂表面上的氧是光生电子e-的主要俘获剂,是e-的有效接受体,氧与e-的还原反应不仅生成表面光催化氧化反应所需的羟基自由基(·OH),而且为空穴提供所需的OH-和H2O,进一步生成·OH,形成一个良性的表面光催化过程,减少半导体光催化剂表面电子-空穴对的复合率,大大提高反应速率。其反应机理如下:  The invention fully considers that the photocatalytic reaction is carried out, and the wastewater is sprayed and oxygenated. When the photocatalytic oxidation reaction proceeds, the participation of O 2 is extremely important. The oxygen adsorbed on the surface of the catalyst is the main capture agent of photogenerated electron e - and the effective acceptor of e - . The reduction reaction of oxygen and e - not only generates surface photocatalytic Hydroxyl radicals (·OH) required for the oxidation reaction, and provide the required OH - and H 2 O for holes, and further generate ·OH, forming a benign surface photocatalytic process, reducing the surface electron-holes of semiconductor photocatalysts The right recombination rate greatly increases the reaction rate. Its reaction mechanism is as follows:

O2+TiO2(e-)→TiO2+·O2 - O 2 +TiO 2 (e - )→TiO 2 +·O 2 -

·O2 -+2H2O+TiO2(e-)→TiO2+H2O2+2OH- ·O 2 - +2H 2 O+TiO 2 (e - )→TiO 2 +H 2 O 2 +2OH -

H2O2+TiO2(e-)→TiO2+·OH+OH- H 2 O 2 +TiO 2 (e - )→TiO 2 +·OH+OH -

TiO2(h+)+H2O→TiO2+H++·OH  TiO 2 (h + )+H 2 O→TiO 2 +H + + OH

TiO2(h+)+OH-→TiO2+·OH  TiO 2 (h + )+OH - →TiO 2 +·OH

下面结合实施例对本发明作进一步说明。  The present invention will be further described below in conjunction with embodiment. the

反应器外筒高度450mm,直径150mm,内筒高度400mm,直径110mm,轴心石英管高度500mm,直径55mm,内置36W中压汞灯,填充135g纳米晶二氧化钛纤维,采用20w水泵,调节反应器过水流量为7L/min,内筒水流上升速度约为2cm/min,1天可循环处理500L浓度为20mg/L的X-3B活性艳红染料废水,耗电量仅为1.32度/天。  The height of the outer cylinder of the reactor is 450mm, and the diameter is 150mm. The height of the inner cylinder is 400mm, and the diameter is 110mm. The water flow rate is 7L/min, and the rising speed of the water flow in the inner cylinder is about 2cm/min. It can recycle 500L of X-3B reactive brilliant red dye wastewater with a concentration of 20mg/L in one day, and the power consumption is only 1.32 kWh/day. the

Claims (5)

1.一种利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置,其特征在于:由纳米晶二氧化钛纤维光催化反应器[1]、储水池[2]、水泵[3]、第一阀门[4]、流量计[5]、第二阀门[6]和喷淋曝气头[7]构成水循环回路;其中,储水池[2]出水口与水泵[3]进水口相连,水泵[3]出水口分为两路,其中一路与第一阀门[4]连接,另一路与第二阀门[6]相连,第一阀门[4]与流量计[5]进水口相连,流量计[5]出水口与纳米晶二氧化钛纤维光催化反应器[1]进水口相连,纳米晶二氧化钛纤维光催化反应器[1]出水口通过管道通向储水池[2]上方,第二阀门[6]与喷淋曝气头[7]相连,喷淋曝气头[7]位于储水池[2]上方;纳米晶二氧化钛纤维光催化反应器[1]包括外筒[10]、内筒[11]、石英管[12]、紫外灯[13]、纳米晶二氧化钛纤维[14]、进水管口[15]、多孔布流板[16]、出水管口[17]、有机纤维棉过滤层[18]和石英管夹具[19];外筒[10]、内筒[11]和石英管[12]由外而内呈同心圆布置;外筒[10]和内筒[11]竖向放置,两者上口均为通口,且外筒[10]上口高度高于内筒[11]上口高度,外筒[10]下口高度也高于内筒[11]下口高度,外筒[10]下口设有一出水管口[17],外筒[10]与内筒[11]之间的环形间隙底部周圈封闭;进水管口[15]呈直径逐渐扩大的圆锥形,并与内筒[11]下口相连,交界处设有多孔布流板[16],多孔布流板[16]上方铺设一层有机纤维棉过滤层[18-1];沿内筒轴心方向设有石英管[12],石英管[12]下口封闭,石英管[12]最底部与有机纤维棉过滤层[18-1]接触,石英管[12]上口为通口,石英管[12]上口高度高于外筒[10]上口高度;石英管[12]内置有紫外灯[13];内筒[11]和石英管[12]之间填充纳米晶二氧化钛纤维[14],内筒[11]上口出水位置再铺设一层有机纤维棉过滤层[18-2]。 1. A circulating water treatment device using a nanocrystalline titanium dioxide fiber photocatalytic reactor, characterized in that: it consists of a nanocrystalline titanium dioxide fiber photocatalytic reactor [1], a water storage tank [2], a water pump [3], and a first valve [4], flow meter [5], second valve [6] and spray aerator head [7] form a water circulation circuit; wherein, the water outlet of the water storage tank [2] is connected with the water inlet of the water pump [3], and the water pump [3] ] The water outlet is divided into two routes, one of which is connected with the first valve [4], the other is connected with the second valve [6], the first valve [4] is connected with the water inlet of the flowmeter [5], and the flowmeter [5] ] The water outlet is connected to the water inlet of the nanocrystalline titanium dioxide fiber photocatalytic reactor [1]. The spray aeration head [7] is connected, and the spray aeration head [7] is located above the water storage tank [2]; the nanocrystalline titanium dioxide fiber photocatalytic reactor [1] includes an outer cylinder [10], an inner cylinder [11], Quartz tube[12], ultraviolet lamp[13], nanocrystalline titanium dioxide fiber[14], water inlet nozzle[15], porous distribution plate[16], outlet nozzle[17], organic fiber cotton filter layer[18] and quartz tube fixture [19]; outer cylinder [10], inner cylinder [11] and quartz tube [12] are arranged in concentric circles from outside to inside; outer cylinder [10] and inner cylinder [11] are placed vertically, two Both the upper openings are through openings, and the height of the upper opening of the outer cylinder [10] is higher than that of the upper opening of the inner cylinder [11], and the height of the lower opening of the outer cylinder [10] is also higher than that of the lower opening of the inner cylinder [11]. [10] The lower mouth is provided with a water outlet pipe mouth [17], and the bottom circumference of the annular gap between the outer cylinder [10] and the inner cylinder [11] is closed; the water inlet pipe mouth [15] is conical in diameter gradually expanding, and It is connected with the lower opening of the inner cylinder [11], and a porous flow distribution plate [16] is provided at the junction, and a layer of organic fiber cotton filter layer [18-1] is laid on the top of the porous flow distribution plate [16]; along the axial direction of the inner cylinder A quartz tube [12] is provided, the bottom of the quartz tube [12] is closed, the bottom of the quartz tube [12] is in contact with the organic fiber cotton filter layer [18-1], the upper port of the quartz tube [12] is a through port, and the quartz tube [12] [12] The height of the upper opening is higher than that of the outer cylinder [10]; the quartz tube [12] has a built-in ultraviolet lamp [13]; the inner cylinder [11] and the quartz tube [12] are filled with nanocrystalline titanium dioxide fibers [14] ], an organic fiber cotton filter layer [18-2] is laid on the water outlet position of the inner cylinder [11]. 2.根据权利要求1所述的利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置,其特征在于:石英管[12]通过夹具[19]夹持定位,其中处于内筒[11]下部和上部位置的第一夹具[19-1]和第二夹具[19-2],分别夹持住石英管[12]并使其固定于内筒[11]的轴心方向,处于最顶端位置的第三夹具[19-3]夹持住石英管[12]并与外筒[10]的上口周圈用螺丝固定,以使石英管[12]上下位置固定。 2. The circulating water treatment device utilizing nanocrystalline titanium dioxide fiber photocatalytic reactor according to claim 1, characterized in that: the quartz tube [12] is clamped and positioned by a clamp [19], wherein it is located at the bottom of the inner cylinder [11] And the first clamp [19-1] and the second clamp [19-2] in the upper position respectively clamp the quartz tube [12] and fix it in the axial direction of the inner cylinder [11], and are at the topmost position The third clamp [19-3] clamps the quartz tube [12] and is fixed with the upper opening circle of the urceolus [10] with screws, so that the upper and lower positions of the quartz tube [12] are fixed. 3.根据权利要求1所述的利用纳米晶二氧化钛纤维光催化反应 器的循环水处理装置,其特征在于:外筒[10]和内筒[11]均为直形圆筒。 3. The circulating water treatment device utilizing nanocrystalline titanium dioxide fiber photocatalytic reactor according to claim 1, characterized in that: the outer cylinder [10] and the inner cylinder [11] are straight cylinders. 4.根据权利要求1所述的利用纳米晶二氧化钛纤维光催化反应器的循环水处理装置,其特征在于:多孔布流板[16]为均匀布有1-3mm小孔的圆形平板,达到均匀分布水流的作用。 4. the circulating water treatment device utilizing nanocrystalline titanium dioxide fiber photocatalytic reactor according to claim 1, characterized in that: the porous flow distribution plate [16] is a circular flat plate evenly distributed with 1-3mm apertures, reaching The effect of evenly distributing the water flow. 5.一种利用纳米晶二氧化钛纤维光催化反应器的循环水处理工艺,其特征在于为:将含有机污染物的废水注入储水池[2]内,开启水泵[3]和紫外灯[13],废水则从储水池[2]左端经水泵[3]泵出,泵出的水分为左右两路,其中左路水经第一阀门[4]调节流量后流经流量计[5],通过扩径圆锥形进水管口[15]流入纳米晶二氧化钛纤维光催化反应器[1]的内筒[11],由于进水管口的直径逐渐扩大,水流横截面积相应扩大,水流速度显著降低,再经多孔布流板[16]和有机纤维棉过滤层[18-1]进一步均匀布流后,水流平稳缓慢上升,流经被紫外灯[13]照射的纳米晶二氧化钛纤维[14]的间隙,在纤维表面发生光催化反应,水中有机污染物得以降解和矿化,水流上升至内筒[11]上方,经有机纤维棉过滤层[18-2]过滤后,沿内筒[11]的上口周圈溢流而下,流至内筒[11]和外筒[10]的间隙底部,经出水管口[17]流出反应器[1],最后自流回储水池[2]的右端;水泵[3]泵出的右路水经第二阀门[6]控制流量后,直接到达储水池[2]右上方的喷淋曝气头[7],从喷淋曝气头[7]的多个小孔射流喷出,进行曝气充氧,富含溶解氧的废水喷入储水池[2]右端,再流向左端经水泵[3]泵出,形成循环。  5. A circulating water treatment process using a nanocrystalline titanium dioxide fiber photocatalytic reactor, characterized in that: inject waste water containing organic pollutants into the storage tank [2], turn on the water pump [3] and the ultraviolet lamp [13] , the waste water is pumped out from the left end of the reservoir [2] through the water pump [3], and the pumped water is divided into left and right paths, in which the water in the left path flows through the flowmeter [5] after being adjusted by the first valve [4]. The diameter-expanding conical water inlet nozzle [15] flows into the inner cylinder [11] of the nanocrystalline titanium dioxide fiber photocatalytic reactor [1]. As the diameter of the water inlet nozzle gradually expands, the cross-sectional area of the water flow increases accordingly, and the water flow velocity decreases significantly. After the porous flow distribution plate [16] and the organic fiber cotton filter layer [18-1] further uniformly distribute the flow, the water flow rises steadily and slowly, and flows through the gap of the nanocrystalline titanium dioxide fiber [14] irradiated by the ultraviolet lamp [13]. , the photocatalytic reaction occurs on the surface of the fiber, the organic pollutants in the water are degraded and mineralized, the water flow rises above the inner cylinder [11], after being filtered by the organic fiber cotton filter layer [18-2], along the inner cylinder [11] The upper circle overflows down, flows to the bottom of the gap between the inner cylinder [11] and the outer cylinder [10], flows out of the reactor [1] through the outlet pipe [17], and finally flows back to the right end of the water storage tank [2] ; The right water pumped by the water pump [3] directly reaches the spray aerator head [7] on the top right of the water storage tank [2] after the flow is controlled by the second valve [6]. A plurality of small hole jets are ejected for aeration and oxygenation, and the wastewater rich in dissolved oxygen is sprayed into the right end of the storage tank [2], and then flows to the left end and is pumped out by the water pump [3] to form a cycle. the
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JP2015514001A (en) * 2012-03-21 2015-05-18 ソウル バイオシス カンパニー リミテッドSeoul Viosys Co.,Ltd. Water purification system using ultraviolet LED
CN103992000A (en) * 2014-04-10 2014-08-20 东莞市赛德工业设计有限公司 Multi-cycle filtered water purifier
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CN114229950B (en) * 2022-01-12 2023-04-18 河海大学 Reactor for continuous flow photocatalytic degradation of organic micropollutants
CN114684984B (en) * 2022-04-12 2023-03-24 安徽钰隆新能源科技集团有限公司 Photocatalytic Reactors for Water Treatment
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Citations (5)

* 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
CN1508073A (en) * 2002-12-19 2004-06-30 石油大学(北京) Fluidized photocatalytic reactor and process for purifying waste water using the reactor
CN101786715A (en) * 2010-03-08 2010-07-28 九江学院 Titanium dioxide precoated dynamic membrane photocatalytic water treatment device
CN101786688A (en) * 2010-02-04 2010-07-28 山东大学 All-weather titanium dioxide nanowire photocatalysis sewage disinfecting and purifying device
CN101831728A (en) * 2010-04-12 2010-09-15 南京理工大学 Method for preparing nano-crystalline photocatalysis titanium dioxide fiber

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080142452A1 (en) * 2006-08-01 2008-06-19 Vortex Corporation Apparatus and method for preventing biological regrowth in water

Patent Citations (5)

* 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
CN1508073A (en) * 2002-12-19 2004-06-30 石油大学(北京) Fluidized photocatalytic reactor and process for purifying waste water using the reactor
CN101786688A (en) * 2010-02-04 2010-07-28 山东大学 All-weather titanium dioxide nanowire photocatalysis sewage disinfecting and purifying device
CN101786715A (en) * 2010-03-08 2010-07-28 九江学院 Titanium dioxide precoated dynamic membrane photocatalytic water treatment device
CN101831728A (en) * 2010-04-12 2010-09-15 南京理工大学 Method for preparing nano-crystalline photocatalysis titanium dioxide fiber

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