[go: up one dir, main page]

CN102976475B - Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst - Google Patents

Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst Download PDF

Info

Publication number
CN102976475B
CN102976475B CN201210554996.1A CN201210554996A CN102976475B CN 102976475 B CN102976475 B CN 102976475B CN 201210554996 A CN201210554996 A CN 201210554996A CN 102976475 B CN102976475 B CN 102976475B
Authority
CN
China
Prior art keywords
water treatment
manganese dioxide
fluorine
composite material
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201210554996.1A
Other languages
Chinese (zh)
Other versions
CN102976475A (en
Inventor
董玉明
李坤
蒋平平
王光丽
赵辉
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.)
Jiangnan University
Original Assignee
Jiangnan 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 Jiangnan University filed Critical Jiangnan University
Priority to CN201210554996.1A priority Critical patent/CN102976475B/en
Publication of CN102976475A publication Critical patent/CN102976475A/en
Application granted granted Critical
Publication of CN102976475B publication Critical patent/CN102976475B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Catalysts (AREA)

Abstract

本发明提出一种以掺杂氟的二氧化锰纳米复合材料为催化剂的臭氧化水处理方法,在含有苯酚类有机物的废水中加入所制入掺杂氟的二氧化锰纳米复合材料做为催化剂以促进臭氧对苯酚类有机污染物的降解,并在此基础上提出了一种新型的臭氧化水处理方法。该方法属于水处理和环境催化技术领域。所得掺杂氟的二氧化锰纳米纳米复合材料引入了非金属元素氟,具有合成步骤易操作、尺度小、在水溶液体系中分散性好、更易于回收等特点,在臭氧化水处理应用中具有广阔的前景。

The present invention proposes an ozonated water treatment method using fluorine-doped manganese dioxide nanocomposite material as a catalyst, adding the prepared fluorine-doped manganese dioxide nanocomposite material as a catalyst in wastewater containing phenolic organic matter In order to promote the degradation of phenolic organic pollutants by ozone, and on this basis, a new ozonated water treatment method was proposed. The method belongs to the technical field of water treatment and environmental catalysis. The obtained fluorine-doped manganese dioxide nano-nanocomposite material introduces the non-metallic element fluorine, and has the characteristics of easy operation of synthesis steps, small scale, good dispersion in aqueous solution system, and easier recovery. It has great potential in ozonated water treatment applications. Broad prospects.

Description

一种以掺杂氟的二氧化锰纳米复合材料为催化剂的臭氧化水处理方法Ozonation water treatment method using fluorine-doped manganese dioxide nanocomposite as catalyst

技术领域 technical field

本发明提出一种以掺杂氟的二氧化锰纳米复合材料为催化剂的臭氧化水处理方法来降低水污染,属于环境催化和水处理领域。  The invention proposes an ozonated water treatment method using a fluorine-doped manganese dioxide nanocomposite material as a catalyst to reduce water pollution, and belongs to the field of environmental catalysis and water treatment. the

背景技术Background technique

当下,工业不断进步,但是不可避免的产生很多污染。做为广泛应用于药物、染料、纤维、酚醛树脂合成以及医药消毒剂等领域的重要工业原料,苯酚在国内外的使用量一直处于上升的趋势。苯酚由于对中枢神经有抑制能力并会损坏肾功能,被认为是一种高毒类物质。由于苯酚的结构问题,各类工厂排出的废水中的酚类物质极难自然降解。臭氧本身具有一定氧化能力,且易于分解,是降解各类有机化合物理想的氧化剂。但是由于臭氧单独氧化有反应速率慢、降解范围窄、矿化率低等问题,在臭氧氧化过程中加入催化剂的催化臭氧化反应有其独特的应用前景。  At present, the industry continues to progress, but inevitably produces a lot of pollution. As an important industrial raw material widely used in the fields of drugs, dyes, fibers, phenolic resin synthesis, and medical disinfectants, the usage of phenol at home and abroad has been on the rise. Phenol is considered a highly toxic substance due to its inhibitory ability to the central nervous system and damage to kidney function. Due to the structural problems of phenol, the phenolic substances in the wastewater discharged from various factories are extremely difficult to degrade naturally. Ozone itself has a certain oxidation ability and is easy to decompose. It is an ideal oxidant for degrading various organic compounds. However, due to the slow reaction rate, narrow degradation range, and low mineralization rate of ozone oxidation alone, the catalytic ozonation reaction with catalyst added in the ozone oxidation process has its unique application prospects. the

催化臭氧化反应是一种高级氧化反应,是对传统非催化臭氧氧化反应的改进和加强。它通过催化剂的作用,提高臭氧氧化的能力,使有机物在较短的时间内降解、矿化。在催化臭氧氧化降解过程中,催化剂起到两方面作用:一是提高臭氧的反应活性和利用率;二是提高有机物的降解速率和矿化程度。相比于均相催化臭氧化反应,多相催化臭氧化反应具有对臭氧分解速率高、催化剂易于回收再利用、无二次污染等优点,已经在要求愈来愈严格的环保处理中得到广泛认可。  The catalytic ozonation reaction is an advanced oxidation reaction, which is an improvement and enhancement of the traditional non-catalytic ozonation reaction. Through the action of catalyst, it improves the ability of ozone oxidation, so that organic matter can be degraded and mineralized in a short period of time. In the process of catalytic ozone oxidation degradation, the catalyst plays two roles: one is to increase the reactivity and utilization rate of ozone; the other is to increase the degradation rate and mineralization degree of organic matter. Compared with the homogeneous catalytic ozonation reaction, the heterogeneous catalytic ozonation reaction has the advantages of high ozone decomposition rate, easy recovery and reuse of the catalyst, and no secondary pollution. It has been widely recognized in the increasingly stringent environmental protection treatment . the

发明内容Contents of the invention

本发明的目的在于提供一种高效的纳米复合材料,并提供其在臭氧化水处理中的使用方法,进而提高催化臭氧化在水处理领域的实际应用价值。本发明的目的可以通过以下技术方案实现:  The purpose of the present invention is to provide a high-efficiency nanocomposite material, and provide its use method in ozonated water treatment, and then improve the practical application value of catalytic ozonation in the field of water treatment. The purpose of the present invention can be achieved through the following technical solutions:

(1)掺杂氟的二氧化锰纳米复合材料的制备:将9mmolKMnO4、6mmol MnCl2.4H2O分别溶于80mL、20mL水中,然后将MnCl2以2.4mL/min的速率逐滴加入到KMnO4溶液中,搅拌一个小时,此时再将10mL不同浓度的NH4F溶液以2.0mL/min的速率滴加到反应液中,继续搅拌一个小时后,将反应液转移到水热反应釜中并在将160℃下反应6h,得到的产品水洗至中性,80℃干燥18h,得到最终的纳米复合材料;  (1) Preparation of fluorine-doped manganese dioxide nanocomposites: 9mmol KMnO 4 and 6mmol MnCl 2 .4H 2 O were dissolved in 80mL and 20mL water respectively, and then MnCl 2 was added dropwise at a rate of 2.4mL/min to KMnO 4 solution, stirred for one hour, at this time, 10 mL of NH 4 F solutions of different concentrations were added dropwise to the reaction solution at a rate of 2.0 mL/min, and after stirring for one hour, the reaction solution was transferred to the hydrothermal reaction kettle and reacted at 160°C for 6h, the obtained product was washed to neutral, and dried at 80°C for 18h to obtain the final nanocomposite material;

(2)臭氧化水处理:将所得纳米复合材料加入到废水中,搅拌下通入臭氧,催化氧化降解有机污染物。  (2) Ozonated water treatment: Add the obtained nano-composite material into the waste water, pass ozone under stirring, and catalyze and oxidize and degrade organic pollutants. the

在实验过程中,其复合材料制备中所用NH4F溶液的浓度为0.2-0.8mol.L-1,添加 催化剂的质量与所处理废水的质量之比为1∶1000,反应温度为25℃时可达到较好的催化效果。  During the experiment, the concentration of the NH 4 F solution used in the preparation of the composite material was 0.2-0.8mol.L -1 , the ratio of the mass of the added catalyst to the mass of the treated wastewater was 1:1000, and the reaction temperature was 25°C A better catalytic effect can be achieved.

本发明的显著特点:  Salient features of the present invention:

(1)掺杂氟的二氧化锰纳米复合材料引入了非金属元素,显著提高了纳米复合材料在臭氧对含苯酚类废水的降解。其催化作用除了来源于纳米复合材料中二氧化锰相以外,掺杂的氟元素也有效的促进了纳米复合材料与臭氧的作用,最终得到较好的催化效果。  (1) The fluorine-doped manganese dioxide nanocomposite material introduces non-metallic elements, which significantly improves the degradation of phenol-containing wastewater by nanocomposite material in ozone. In addition to its catalytic effect originating from the manganese dioxide phase in the nanocomposite material, the doped fluorine element also effectively promotes the interaction between the nanocomposite material and ozone, and finally obtains a better catalytic effect. the

(2)掺杂氟的二氧化锰纳米复合材料尺寸较小,在水中易于分散,使得纳米复合材料与臭氧以及苯酚类污染物的接触面积增大,最大程度的利用了促进了污染物的降解。  (2) The fluorine-doped manganese dioxide nanocomposite has a small size and is easy to disperse in water, which increases the contact area between the nanocomposite and ozone and phenol pollutants, and maximizes the use of pollutants to degrade them. . the

(3)掺杂氟的二氧化锰纳米复合材料合成过程简单环保,合成过程中无二次污染,且通过简单的沉降即可回收再利用,为其实际应用提供了重要保证。  (3) The synthesis process of fluorine-doped manganese dioxide nanocomposites is simple and environmentally friendly, there is no secondary pollution during the synthesis process, and it can be recycled and reused through simple sedimentation, which provides an important guarantee for its practical application. the

附图说明Description of drawings

图1中(a)、(b)、(c)、(d)分别为实施例1,2,3,4所得产品的SEM照片;  Among Fig. 1 (a), (b), (c), (d) are the SEM photo of embodiment 1,2,3,4 obtained product respectively;

图2中a、b、c、d分别为实施例1,2,3,4所得产品的XRD图谱;  Among Fig. 2, a, b, c, d are the XRD collection of illustrative plates of embodiment 1,2,3,4 obtained products respectively;

图3为实施例6中苯酚随臭氧化时间的浓度变化曲线,a线为单独臭氧化(无催化剂),b线为实施例1中纳米材料催化臭氧化,c线为实施例2中纳米材料催化臭氧化,d线为实施例3中纳米材料催化臭氧化,e线为实施例4纳米材料催化臭氧化,  Fig. 3 is the concentration variation curve of phenol with ozonation time in embodiment 6, a line is ozonation alone (without catalyst), b line is nanomaterial catalyzed ozonation in embodiment 1, and c line is nanomaterial in embodiment 2 Catalytic ozonation, d line is the catalytic ozonation of nanomaterials in embodiment 3, and e line is the catalytic ozonation of nanomaterials in embodiment 4,

具体实施方式Detailed ways

为了更具体的说明本发明的方法,下面给出本发明的实施例,但本发明的应用不限于此。  In order to describe the method of the present invention more specifically, the following examples of the present invention are given, but the application of the present invention is not limited thereto. the

实施例1  Example 1

称取9mmolKMnO4,将其溶于80mL水中,然后用磁力搅拌器将其搅拌均匀。称取6mmol MnCl2.4H2O溶于20mL水中,然后将其以2.4mL/min的速率逐滴加入到前述已经溶解、搅拌好的KMnO4溶液中。待滴加完毕后,继续搅拌1h,然后以2.0ml/nin的速率将15mL已经提前配置好的0.2mol.L-1的NH4F溶液滴加到前述已经反应1h的溶液中。待NH4F溶液全部滴加完毕,继续在相同的速率下搅拌1h后,将反应液转移到120mL的水热反应釜中,并在160℃下反应6h。水热反应完毕后,将反应釜自然冷却至室温,得到的产物水洗至中性,在80℃下干燥18h至干燥,得到最终的纳米材料。  Weigh 9mmol KMnO 4 , dissolve it in 80mL water, and stir it evenly with a magnetic stirrer. Weigh 6 mmol of MnCl 2 .4H 2 O and dissolve it in 20 mL of water, and then add it dropwise at a rate of 2.4 mL/min to the previously dissolved and stirred KMnO 4 solution. After the dropwise addition, continue to stir for 1 h, and then add 15 mL of 0.2 mol.L -1 NH 4 F solution prepared in advance at a rate of 2.0 ml/min to the aforementioned solution that has been reacted for 1 h. After all the NH 4 F solution was added dropwise, the reaction solution was transferred to a 120 mL hydrothermal reactor and reacted at 160° C. for 6 h after continuing to stir at the same rate for 1 h. After the completion of the hydrothermal reaction, the reactor was naturally cooled to room temperature, and the obtained product was washed to neutrality, and dried at 80° C. for 18 hours to obtain the final nanomaterial.

实施例2  Example 2

称取9mmol KMnO4,将其溶于80mL水中,然后用磁力搅拌器将其搅拌均匀。称取6mmol MnCl2·4H2O溶于20mL水中,然后将其以2.4mL/min的速率逐滴加入到前述已经溶解、搅拌好的KMnO4溶液中。待滴加完毕后,继续搅拌1h,然后以2.0mL/min的速率将15mL已经提前配置好的0.4mol·L-1的NH4F溶液滴加到前述已经反应1h的溶液中。待NH4F溶液全部滴加完毕,继续在相同的速率下搅拌1h后,将反应液转移到120mL的水热反应釜中,并在160℃下反应6h。水热反应完毕后,将反应釜自然冷却至室温,得到的产物水洗至中性,在80℃下干燥18h至干燥,得到最终的纳米材料。  Weigh 9mmol KMnO 4 , dissolve it in 80mL water, and stir it evenly with a magnetic stirrer. Weigh 6 mmol of MnCl 2 ·4H 2 O and dissolve it in 20 mL of water, and then add it dropwise at a rate of 2.4 mL/min to the previously dissolved and stirred KMnO 4 solution. After the dropwise addition was completed, the stirring was continued for 1 h, and then 15 mL of 0.4 mol·L -1 NH 4 F solution prepared in advance was added dropwise at a rate of 2.0 mL/min to the aforementioned solution that had been reacted for 1 h. After all the NH 4 F solution was added dropwise, the reaction solution was transferred to a 120 mL hydrothermal reactor and reacted at 160° C. for 6 h after continuing to stir at the same rate for 1 h. After the completion of the hydrothermal reaction, the reactor was naturally cooled to room temperature, and the obtained product was washed to neutrality, and dried at 80° C. for 18 hours to obtain the final nanomaterial.

实施例3  Example 3

称取9mmol KMnO4,将其溶于80mL水中,然后用磁力搅拌器将其搅拌均匀。称取6mmol MnCl2·4H2O溶于20mL水中,然后将其以2.4mL/min的速率逐滴加入到前述已经溶解、搅拌好的KMnO4溶液中。待滴加完毕后,继续搅拌1h,然后以2.0mL/min的速率将15mL已经提前配置好的0.6mol·L-1的NH4F溶液滴加到前述已经反应1h的溶液中。待NH4F溶液全部滴加完毕,继续在相同的速率下搅拌1h后,将反应液转移到120mL的水热反应釜中,并在160℃下反应6h。水热反应完毕后,将反应釜自然冷却至室温,得到的产物水洗至中性,在80℃下干燥18h至干燥,得到最终的纳米材料。  Weigh 9mmol KMnO 4 , dissolve it in 80mL water, and stir it evenly with a magnetic stirrer. Weigh 6 mmol of MnCl 2 ·4H 2 O and dissolve it in 20 mL of water, and then add it dropwise at a rate of 2.4 mL/min to the previously dissolved and stirred KMnO 4 solution. After the dropwise addition was completed, the stirring was continued for 1 h, and then 15 mL of 0.6 mol·L -1 NH 4 F solution that had been prepared in advance was added dropwise at a rate of 2.0 mL/min to the aforementioned solution that had been reacted for 1 h. After all the NH 4 F solution was added dropwise, the reaction solution was transferred to a 120 mL hydrothermal reactor and reacted at 160° C. for 6 h after continuing to stir at the same rate for 1 h. After the completion of the hydrothermal reaction, the reactor was naturally cooled to room temperature, and the obtained product was washed to neutrality, and dried at 80° C. for 18 hours to obtain the final nanomaterial.

实施例4  Example 4

称取9mmol KMnO4,将其溶于80mL水中,然后用磁力搅拌器将其搅拌均匀。称取6mmol MnCl2·4H2O溶于20mL水中,然后将其以2.4mL/min的速率逐滴加入到前述已经溶解、搅拌好的KMnO4溶液中。待滴加完毕后,继续搅拌1h,然后以2.0mL/min的速率将15mL已经提前配置好的0.8mol·L-1的NH4F溶液滴加到前述已经反应1h的溶液中。待NH4F溶液全部滴加完毕,继续在相同的速率下搅拌1h后,将反应液转移到120mL的水热反应釜中,并在160℃下反应6h。水热反应完毕后,将反应釜自然冷却至室温,得到的产物水洗至中性,在80℃下干燥18h至干燥,得到最终的纳米材料。  Weigh 9mmol KMnO 4 , dissolve it in 80mL water, and stir it evenly with a magnetic stirrer. Weigh 6 mmol of MnCl 2 ·4H 2 O and dissolve it in 20 mL of water, and then add it dropwise at a rate of 2.4 mL/min to the previously dissolved and stirred KMnO 4 solution. After the dropwise addition was completed, the stirring was continued for 1 h, and then 15 mL of 0.8 mol·L -1 NH 4 F solution prepared in advance was added dropwise at a rate of 2.0 mL/min to the aforementioned solution that had been reacted for 1 h. After all the NH 4 F solution was added dropwise, the reaction solution was transferred to a 120 mL hydrothermal reactor and reacted at 160° C. for 6 h after continuing to stir at the same rate for 1 h. After the completion of the hydrothermal reaction, the reactor was naturally cooled to room temperature, and the obtained product was washed to neutrality, and dried at 80° C. for 18 hours to obtain the final nanomaterial.

实施例5  Example 5

量取苯酚含量为300mg L-1的模拟废水200mL,添加上述实施例得到的纳米复合 材料0.20g,使用磁力搅拌匀速搅拌10分钟以后,在25℃下通入流量为21mL/min的臭氧。每隔相同的时间段取样,测试苯酚的浓度。结果如图3所示。说明本发明的纳米复合材料对含苯酚类废水有显著的催化作用。  Measure 200 mL of simulated wastewater with a phenol content of 300 mg L -1 , add 0.20 g of the nanocomposite material obtained in the above example, and stir at a constant speed for 10 minutes using a magnetic stirrer, then inject ozone at a flow rate of 21 mL/min at 25 °C. Samples were taken at equal intervals to test the concentration of phenol. The result is shown in Figure 3. It shows that the nanocomposite material of the present invention has significant catalytic effect on wastewater containing phenols.

Claims (2)

1. the ozonization water treatment method take the manganese dioxide nano-composite material of doped with fluorine as catalyzer, is characterized in that adopting the nano material of nonmetal doping as catalyzer, and concrete steps are as follows:
(1) preparation of the manganese dioxide nano-composite material of doped with fluorine: by 9mmolKMnO 4and 6mmolMnCl 2.4H 2o is dissolved in respectively in 80mL, 20mL water, under the condition of magnetic agitation, by MnCl 2the aqueous solution be dropwise added drop-wise to KMnO with the speed of 2.4mL/min 4in solution, continue after one hour, in reaction solution, to add the certain density NH of 15mL with the speed of 2.0mL/min with constant speed stirring reaction liquid 4f solution, then transfers to reaction solution in the hydrothermal reaction kettle of 120mL, and reacts 6h at 160 ℃, after reaction finishes, reactor is naturally cooled to room temperature, and the product water obtaining is washed till neutrality, and 80 ℃ of dry 18h, obtain final nano composite material;
(2) ozonization water treatment: synthetic nano composite material is joined in waste water, pass into ozone under stirring, catalyzing oxidizing degrading organic pollutant.
2. the manganese dioxide nano-composite material take doped with fluorine according to claim 1 is the ozonization water treatment method of catalyzer, NH used in its matrix material preparation 4the concentration of F solution is 0.2-0.8mol.L -1.
CN201210554996.1A 2012-12-20 2012-12-20 Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst Expired - Fee Related CN102976475B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210554996.1A CN102976475B (en) 2012-12-20 2012-12-20 Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210554996.1A CN102976475B (en) 2012-12-20 2012-12-20 Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst

Publications (2)

Publication Number Publication Date
CN102976475A CN102976475A (en) 2013-03-20
CN102976475B true CN102976475B (en) 2014-06-04

Family

ID=47850893

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210554996.1A Expired - Fee Related CN102976475B (en) 2012-12-20 2012-12-20 Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst

Country Status (1)

Country Link
CN (1) CN102976475B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107359052A (en) * 2017-07-03 2017-11-17 武汉纽赛儿科技股份有限公司 The synthetic method of Fluorin doped carbon coating manganese oxide and its application
CN109250801A (en) * 2018-10-24 2019-01-22 大连理工大学 A kind of processing method of phenolic waste water
CN110227484B (en) * 2019-07-16 2023-11-28 河北工业大学 A doped nano-manganese dioxide composite material, preparation method and application
CN113332975A (en) * 2021-04-15 2021-09-03 浙江大学 Honeycomb ceramic etching supported catalyst and preparation method and application thereof
CN114452987B (en) * 2021-12-28 2024-03-19 浙江理工大学桐乡研究院有限公司 PVDF modified metal oxide catalyst and preparation method and application thereof
CN115245832B (en) * 2021-12-28 2023-12-01 浙江理工大学 Preparation method, product and application of fluorine doped metal oxide catalyst

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6149820A (en) * 1997-10-20 2000-11-21 Haldor Topsoe A/S Catalyst, process and process unit for the abatement of noxious compounds in water
CN1748865A (en) * 2005-08-25 2006-03-22 上海交通大学 Preparation method of fluorine-doped metal oxide catalyst
CN1812835A (en) * 2003-04-29 2006-08-02 约翰逊马西有限公司 Manganese ozone decomposition catalysts and process for its preparation
CN101050036A (en) * 2007-05-21 2007-10-10 哈尔滨工业大学 Method for controlling generation quantity of bromic acid radicle in treating procedure for oxidizing drinking water by ozone
CN101579626A (en) * 2009-06-19 2009-11-18 哈尔滨工业大学 Nanometer manganese ion doping titanium dioxide catalyst and preparation method thereof
CN101891297A (en) * 2010-07-19 2010-11-24 江南大学 A kind of ozonation water treatment method using manganese dioxide one-dimensional nanomaterial as catalyst

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6149820A (en) * 1997-10-20 2000-11-21 Haldor Topsoe A/S Catalyst, process and process unit for the abatement of noxious compounds in water
CN1812835A (en) * 2003-04-29 2006-08-02 约翰逊马西有限公司 Manganese ozone decomposition catalysts and process for its preparation
CN1748865A (en) * 2005-08-25 2006-03-22 上海交通大学 Preparation method of fluorine-doped metal oxide catalyst
CN101050036A (en) * 2007-05-21 2007-10-10 哈尔滨工业大学 Method for controlling generation quantity of bromic acid radicle in treating procedure for oxidizing drinking water by ozone
CN101579626A (en) * 2009-06-19 2009-11-18 哈尔滨工业大学 Nanometer manganese ion doping titanium dioxide catalyst and preparation method thereof
CN101891297A (en) * 2010-07-19 2010-11-24 江南大学 A kind of ozonation water treatment method using manganese dioxide one-dimensional nanomaterial as catalyst

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
董玉明,王光丽等.陶瓷粉体催化臭氧降解水中苯酚.《水处理技术》.2010,第36卷(第10期),28-30. *

Also Published As

Publication number Publication date
CN102976475A (en) 2013-03-20

Similar Documents

Publication Publication Date Title
CN102976475B (en) Ozonization water treatment method by taking fluorine-doped manganese dioxide nano composite material as catalyst
Yu et al. Reactive oxygen species and catalytic active sites in heterogeneous catalytic ozonation for water purification
Zhu et al. Postsynthesis growth of CoOOH nanostructure on SrCo0. 6Ti0. 4O3− δ perovskite surface for enhanced degradation of aqueous organic contaminants
Wu et al. Removal of gaseous volatile organic compounds by a multiwalled carbon nanotubes/peroxymonosulfate wet scrubber
CN101891297B (en) Ozonization water treatment method using manganese dioxide one-dimensional nano material as catalyst
CN104310565B (en) A kind of based on iron-based organic-method of the embryonic stem-like cells process organic waste water of framework material
CN102173500B (en) Method for treating water by Fenton oxidization of activated molecular oxygen
CN102350317B (en) Polypyrrole/titanium dioxide composite adsorbent, its preparation, application and regeneration methods
CN103263910B (en) A kind of pucherite-graphene composite photocatalyst and Synthesis and applications thereof
CN101130169A (en) Preparation of Complex Iron Catalyst and Its Application to Heterogeneous Photocatalysis of Hydrogen Peroxide
CN106238053A (en) A kind of photo-Fenton catalyst Fe3O4/rGO/TiO2 and its preparation method and application
CN110327917B (en) Preparation method of metal-doped manganese dioxide photocatalyst for coking wastewater treatment
CN109248704A (en) Carbon, the preparation of oxygen codope graphite phase carbon nitride and its application in catalytic activation persulfate degradation water pollutant
CN113209970B (en) Preparation method and application of carbon-based catalyst prepared from excess sludge
CN102059146B (en) Catalyst for further treating coking wastewater and preparation method thereof
CN103861571A (en) Preparation method, application and regeneration method of polyaniline and titanium dioxide composite adsorbent
CN102078807A (en) Photocatalyst supporting Er3+:YAlO3/TiO2 and its preparation method
CN101774676A (en) Method for treating high-concentration industrial organic waste water and relevant catalyst
Zhou et al. Highly efficient degradation of tartrazine with a benzoic acid/TiO2 system
CN103285874B (en) Inorganic nano composite catalyst with peroxidase property and application of catalyst for performing catalytic decomposition on TMB thereof
Jiang et al. Tuning band gap in Fe-doped g-C3N4 by Zn for enhanced Fenton-like catalytic performance
CN102659126A (en) Preparation method and application of iron-manganese composite silicate
CN102701426A (en) Method for removing organic matters from source water by catalyzing ozone by using pumice loaded hydroxyl ferric oxide
Li et al. Review of modified biochar for removing humic acid from water: analysis of structure-activity relationship
CN103933980B (en) The preparation method of Polyferro-silicate doping hydroxyl oxidize iron catalyst and application thereof

Legal Events

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

Granted publication date: 20140604

Termination date: 20141220

EXPY Termination of patent right or utility model