CN110614102A - Preparation and application of chlorine-doped zinc oxide nano-rod - Google Patents
Preparation and application of chlorine-doped zinc oxide nano-rod Download PDFInfo
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- CN110614102A CN110614102A CN201911020009.8A CN201911020009A CN110614102A CN 110614102 A CN110614102 A CN 110614102A CN 201911020009 A CN201911020009 A CN 201911020009A CN 110614102 A CN110614102 A CN 110614102A
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- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 title claims abstract description 112
- 239000011787 zinc oxide Substances 0.000 title claims abstract description 56
- 239000002073 nanorod Substances 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- 239000002351 wastewater Substances 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000013033 photocatalytic degradation reaction Methods 0.000 claims abstract description 9
- 229910052984 zinc sulfide Inorganic materials 0.000 claims abstract description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 30
- 238000006243 chemical reaction Methods 0.000 claims description 20
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 18
- 239000003054 catalyst Substances 0.000 claims description 16
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 16
- 239000011592 zinc chloride Substances 0.000 claims description 8
- 235000005074 zinc chloride Nutrition 0.000 claims description 8
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 claims description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 6
- 230000009471 action Effects 0.000 claims description 6
- 239000000460 chlorine Substances 0.000 claims description 6
- 229910052801 chlorine Inorganic materials 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 4
- 238000004729 solvothermal method Methods 0.000 claims description 3
- 238000001179 sorption measurement Methods 0.000 claims description 2
- 238000009210 therapy by ultrasound Methods 0.000 claims description 2
- 229910052724 xenon Inorganic materials 0.000 claims description 2
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 claims description 2
- 239000012295 chemical reaction liquid Substances 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 12
- 230000001699 photocatalysis Effects 0.000 abstract description 12
- 230000015556 catabolic process Effects 0.000 abstract description 11
- 238000006731 degradation reaction Methods 0.000 abstract description 11
- 238000009776 industrial production Methods 0.000 abstract description 3
- 239000002957 persistent organic pollutant Substances 0.000 abstract 1
- 238000004065 wastewater treatment Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 230000001476 alcoholic effect Effects 0.000 description 3
- 239000000969 carrier Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000005067 remediation Methods 0.000 description 3
- 239000004065 semiconductor Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- 239000003570 air Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 230000000593 degrading effect Effects 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000001000 micrograph Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000006557 surface reaction Methods 0.000 description 2
- 231100000167 toxic agent Toxicity 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000002153 concerted effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 238000013032 photocatalytic reaction Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000012876 topography Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/138—Halogens; Compounds thereof with alkaline earth metals, magnesium, beryllium, zinc, cadmium or mercury
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/39—Photocatalytic properties
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
- C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/10—Photocatalysts
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
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Abstract
The invention discloses a preparation method and application of a chlorine-doped zinc oxide nanorod. The prepared chlorine-doped zinc oxide nano rod is of a non-centrosymmetric hexagonal wurtzite structure, can generate a piezoelectric field under the assistance of sound waves, and promotes photocatalytic wastewater treatment. The photocatalytic degradation rate of the chlorine-doped zinc oxide under the assistance of sound waves for wastewater is 0.02315 min‑1The degradation rate is 1.5 times of the photocatalytic wastewater degradation rate of zinc oxide under the assistance of sound waves, and 4.9 times of the single photocatalytic degradation rate of chlorine-doped zinc oxide. The method provided by the invention obviously improves the capacity of the zinc oxide material in photocatalytic degradation of organic pollutants, especially realizes double capture of light energy and mechanical energy, and the preparation method provided by the invention is simple and is suitable for industrial production.
Description
Technical Field
The invention belongs to the technical field of photo-acoustic concerted catalysis, and particularly relates to preparation and application of a chlorine-doped zinc oxide nanorod.
Background
The contemporary world is facing environmental pollution due to rapid global industrialization leading to deterioration of water, air and soil quality due to accumulated organic and inorganic toxic compounds. These toxic compounds have hazardous properties that affect the ecosystem and thus human health. For this reason, remediation of contaminated water, air and soil is essential to improve human survival. Among various environmental remediation methods, the degradation of contaminants by photocatalytic semiconductor materials has been considered as a promising green technology for environmental remediation.
During the photocatalytic reaction, the host of photon-generated carriers is only two types: the complex conversion is thermal and other ineffective energy sources or participates in surface reaction, and the latter is an ideal energy conversion mode. Only when the photo-generated carriers smoothly migrate to the surface of the catalyst and act with the electron donor (acceptor) adsorbed on the surface of the catalyst, the ideal photo-catalytic oxidation (reduction) reaction can occur. In the above process, the separation and migration process of the photon-generated carriers is an intermediate link connecting the semiconductor light excitation and the surface reaction behavior. The improvement of the carrier separation efficiency of the semiconductor catalyst and the acceleration of the interface charge transfer are key scientific problems to be solved for constructing high-efficiency photocatalytic materials and are also the research frontier in the current international photocatalytic field.
Recently, attention has been focused on the use of ferroelectric and piezoelectric materials in photocatalytic technology. When a piezoelectric material is used, the built-in electric field generated by the piezoelectric material under force helps the charge separation. In the photocatalysis and piezoelectric composite materials reported at home and abroad, zinc oxide is widely reported as a star material, but the catalytic efficiency of the zinc oxide needs to be improved, the preparation process is complex, the yield is low, and the industrial production requirements cannot be met.
The invention discloses a new material with better piezoelectric property, which can promote the degradation of photocatalytic dye under the simultaneous action of sound wave and light, and the performance of the new material for catalyzing and degrading polluted wastewater is obviously superior to the action of zinc oxide by independent light or independent sound wave. The material can realize double capture of light energy and mechanical energy, and carry out polluted wastewater degradation under the synergistic drive of sound waves and light waves.
Disclosure of Invention
The invention aims to provide preparation and application of a chlorine-doped zinc oxide nanorod, which combines the photocatalytic property and the piezoelectric property of a material, realizes the auxiliary photocatalytic degradation of polluted wastewater under the action of sound waves, and improves the degradation rate by times.
In order to achieve the purpose, the invention adopts the following technical scheme:
preparation and application of a chlorine-doped zinc oxide nanorod, wherein the crystal belongs to a non-centrosymmetric hexagonal wurtzite structure; the length of the chlorine-doped zinc oxide nano rod is 0.5mm-1mm, and the diameter is 30nm-60 nm.
The preparation method of the piezoelectric catalyst is characterized in that zinc stearate is used as a zinc source, potassium hydroxide is used as an alkali source, zinc chloride is used as a chlorine source, methanol is used as a reaction solvent, and the chlorine-doped zinc oxide nanorod is prepared by an alcohol thermal method. The method specifically comprises the following steps:
(1) the molar ratio of the raw materials is 1: 1, respectively weighing zinc stearate and potassium hydroxide, respectively dissolving the zinc stearate and the potassium hydroxide in methanol, and stirring the solution at normal temperature to prepare alcoholic solutions of two reactants;
(2) slowly mixing the alcoholic solutions of the two reactants prepared in the step (1), stirring for 30 min while mixing, and then weighing the mixture of potassium hydroxide and zinc chloride according to a molar ratio of 1: adding 0.05 part of zinc chloride into the mixed solution, continuously stirring for 30 min to uniformly mix the mixed solution, and transferring the reaction solution into a polytetrafluoroethylene reaction kettle, wherein the solvothermal reaction temperature is 100-200 ℃, and the solvothermal time is 24-72 h;
(3) after the reaction is finished, washing the sample by using ethanol and deionized water, and drying at 60 ℃ for 12 h to prepare the chlorine-doped zinc oxide nano rod.
The application comprises the following steps: under the action of sound waves, the chlorine-doped zinc oxide nanorod catalyst promotes the photocatalytic degradation of RhB wastewater, and specifically comprises the following steps:
1) placing a chlorine-doped zinc oxide nanorod catalyst in a glass reactor, adding RhB wastewater, performing ultrasonic treatment to uniformly disperse the chlorine-doped zinc oxide nanorod catalyst in the RhB wastewater, and placing the reactor in the dark for dark adsorption for 30 minutes under stirring;
2) fixing the reactor in a frequency-controllable sound wave vibration field, applying a xenon lamp light source above the reactor, wherein the power is 300W, and the wavelength is 200-700 nm; the sound vibration is applied below, the sound frequency is controlled between 27 and 40 kHz, and the circulating water is always opened to keep the temperature of the reactor stable at 25 ℃. Samples were taken every 5min and the reaction was stopped after 25 min.
The concentration of the chlorine-doped zinc oxide nanorod catalyst in the glass reactor in the step 1) is 0.2 mg/ml.
The invention has the following remarkable advantages:
(1) the chlorine-doped zinc oxide catalyst adopted by the invention has a crystal structure which belongs to a non-centrosymmetric hexagonal wurtzite structure, is simple in preparation method and is suitable for industrial production;
(2) compared with a non-doped zinc oxide nano rod, the obtained chlorine-doped zinc oxide catalyst has higher piezoelectric performance, so that the capture and conversion of sound energy are facilitated;
(3) the obtained chlorine-doped zinc oxide can assist in photocatalytic degradation of dye under the action of sound waves, wherein the photocatalytic degradation rate can reach 0.02315 min in an ultrasonic field of 40 kHz-1And the degradation rate of the zinc oxide under the same conditions is 0.0151 min-1The degradation rate is 1.5 times of the photocatalytic wastewater degradation rate of zinc oxide under the assistance of sound waves and 4.9 times of the single photocatalytic degradation rate of chlorine-doped zinc oxide, so that the chlorine-doped zinc oxide can be seen in the wastewaterThe performance in terms of treatment is obviously superior to that of the zinc oxide catalyst.
(4) The catalyst prepared by the invention not only can enrich mechanical energy in natural environment, but also can provide a new path for degrading photocatalytic polluted wastewater, and realizes dual capture of light energy and mechanical energy.
Drawings
FIG. 1 is an X-ray diffraction pattern of zinc oxide and chlorine-doped zinc oxide nanorods;
FIG. 2 is a zinc oxide field emission scanning electron microscope image;
FIG. 3 is a field emission scanning electron microscope image of a chlorine-doped zinc oxide nanorod;
figure 4 is a graph of the degradation rate of zinc oxide and chlorine doped zinc oxide nanorods dye.
Detailed Description
In order to make the present invention more comprehensible, the technical solutions of the present invention are further described below with reference to specific embodiments, but the present invention is not limited thereto.
Example 1 Synthesis of Zinc oxide nanorods and chlorine-doped Zinc oxide nanorods by Alcoholic thermal method
0.632 g of zinc stearate (1 mmol) and 0.056 g of potassium hydroxide (1 mmol) are respectively weighed and dissolved in 10 mL and 20 mL of methanol, the reaction solution containing the zinc stearate is dropwise added into the reaction solution containing the potassium hydroxide, and the mixture is fully stirred for 30 min to uniformly mix the precursors. Weighing 6.8 mg (0.05 mmol) of zinc chloride, adding the zinc chloride into the reaction solution, stirring for 30 min to fully dissolve the zinc chloride, transferring the obtained reaction solution into a polytetrafluoroethylene reaction kettle, putting the reaction kettle into a stainless steel sleeve to be locked, placing the reaction kettle into an oven, carrying out solvothermal reaction at the temperature of 100 ℃ and 200 ℃ for 24-72 h, washing a sample by using ethanol and deionized water, and drying at the temperature of 60 ℃ for 12 h to obtain white powder, namely the chlorine-doped zinc oxide nanorod. The preparation process of the zinc oxide nano rod is similar to the above process, and the reaction solution is not added with a chlorine source, so that the zinc oxide nano rod can be obtained.
Example 2 structural characterization
The sample prepared according to example 1 was scanned by an X-ray diffractometer and the results are shown in figure 1. From fig. 1, it can be confirmed that when zinc oxide is doped with chlorine, the crystal structure of the zinc oxide is not changed and is a hexagonal wurtzite structure.
Example 3 topography characterization
The zinc oxide prepared according to the example 1 and the chlorine-doped zinc oxide are observed by a field emission scanning electron microscope, and the results are shown in fig. 2 and fig. 3, and the comparison between the fig. 2 and fig. 3 shows that the shape is not changed when the zinc oxide is doped with chlorine, and the material is a rod-shaped structure with the length of 0.5-1mm and the diameter of 30-60 nm.
Example 4 degradation of RhB simulated polluted wastewater Performance test
10mg of the zinc oxide and chlorine-doped zinc oxide prepared in example 1 were respectively weighed and dispersed in 50 ml of 10ppm RhB simulated polluted wastewater, and the catalytic activity was measured under different conditions: (1) adopting a 300W light source with the wavelength of 365 nm to perform independent illumination; (2) carrying out an independent ultrasonic experiment by adopting 100W 40 kHz ultrasonic frequency; (3) simultaneously light and ultrasound. Samples were taken every 5min and the reaction was stopped after 25 min. The supernatant was centrifuged and the RhB removal rate was measured by Cary 50 uv-vis spectrophotometer and the results are shown in fig. 4.
The above description is only a preferred embodiment of the present invention, and all equivalent changes and modifications made in accordance with the claims of the present invention should be covered by the present invention.
Claims (5)
1. A preparation method of a chlorine-doped zinc oxide nanorod is characterized by comprising the following steps: the length of the chlorine-doped zinc oxide nano rod is 0.5mm-1mm, the diameter is 30nm-60nm, and the structure is a hexagonal wurtzite structure;
the preparation method comprises the following steps:
(1) respectively dissolving zinc stearate and potassium hydroxide in methanol, dropwise adding the methanol solution dissolved with the zinc stearate into the methanol solution dissolved with the potassium hydroxide, and adding the reaction solution by taking zinc chloride as a chlorine source;
(2) and (2) transferring the reaction liquid obtained in the step (1) to a reaction kettle for solvothermal reaction at the temperature of 100 ℃ and 200 ℃ for 24-72 h to obtain the chlorine-doped zinc oxide nanorod.
2. The method of claim 1, wherein: the molar ratio of zinc stearate to potassium hydroxide is 1: 1.
3. the method of claim 1, wherein: the molar ratio of the potassium hydroxide to the zinc chloride is 1: 0.05.
4. the application of the chlorine-doped zinc oxide nanorod prepared by the preparation method according to claim 1 is characterized in that: under the action of sound waves, the chlorine-doped zinc oxide nanorod catalyst promotes the photocatalytic degradation of RhB wastewater, and specifically comprises the following steps:
1) placing a chlorine-doped zinc oxide nanorod catalyst in a glass reactor, adding RhB wastewater, performing ultrasonic treatment to uniformly disperse the chlorine-doped zinc oxide nanorod catalyst in the RhB wastewater, and placing the reactor in the dark for dark adsorption for 30 minutes under stirring; 2) Fixing the reactor in a frequency-controllable sound wave vibration field, applying a xenon lamp light source above the reactor, wherein the power is 300W, and the wavelength is 200-700 nm; applying sound vibration below the reactor, controlling the sound frequency at 27-40 kHz, and opening circulating water all the time to keep the temperature of the reactor stable at 25 ℃ and finishing the reaction after 25 min.
5. Use according to claim 4, characterized in that: the concentration of the chlorine-doped zinc oxide nanorod catalyst in the glass reactor in the step 1) is 0.2 mg/ml.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112010387A (en) * | 2020-08-13 | 2020-12-01 | 西安工程大学 | Method for degrading dye through photocatalysis of rodlike zinc oxide assisted by ultrasound |
CN112108141A (en) * | 2020-08-27 | 2020-12-22 | 南京信息工程大学 | Zinc oxide micron rod piezoelectric catalyst and preparation method and application thereof |
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2019
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112010387A (en) * | 2020-08-13 | 2020-12-01 | 西安工程大学 | Method for degrading dye through photocatalysis of rodlike zinc oxide assisted by ultrasound |
CN112108141A (en) * | 2020-08-27 | 2020-12-22 | 南京信息工程大学 | Zinc oxide micron rod piezoelectric catalyst and preparation method and application thereof |
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