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 PDFInfo
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- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 239000002114 nanocomposite Substances 0.000 title claims abstract description 23
- 239000000463 material Substances 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000006385 ozonation reaction Methods 0.000 title claims description 16
- 239000003054 catalyst Substances 0.000 title abstract description 10
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000002351 wastewater Substances 0.000 claims abstract description 8
- 229910052731 fluorine Inorganic materials 0.000 claims abstract description 5
- 239000011737 fluorine Substances 0.000 claims abstract description 5
- 239000002957 persistent organic pollutant Substances 0.000 claims abstract description 3
- 239000007864 aqueous solution Substances 0.000 claims abstract 2
- 238000003756 stirring Methods 0.000 claims description 17
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 239000002086 nanomaterial Substances 0.000 claims description 9
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 6
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- 230000000593 degrading effect Effects 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 239000000243 solution Substances 0.000 claims 5
- 238000013019 agitation Methods 0.000 claims 1
- 239000012295 chemical reaction liquid Substances 0.000 claims 1
- 239000011159 matrix material Substances 0.000 claims 1
- 229910052755 nonmetal Inorganic materials 0.000 claims 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 abstract description 11
- 230000015556 catabolic process Effects 0.000 abstract description 5
- 238000006731 degradation reaction Methods 0.000 abstract description 5
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 238000003786 synthesis reaction Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000005416 organic matter Substances 0.000 abstract description 3
- 238000006555 catalytic reaction Methods 0.000 abstract description 2
- 229910052751 metal Inorganic materials 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 abstract 1
- 239000006185 dispersion Substances 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 description 14
- 229910017855 NH 4 F Inorganic materials 0.000 description 10
- 238000007254 oxidation reaction Methods 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 230000033558 biomineral tissue development Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 210000003169 central nervous system Anatomy 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000003907 kidney function Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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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
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
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
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
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.
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