Loaded multifunctional catalysis composite material, preparation method thereof and application of composite material to catalytic removal of water pollutants

11207670 · 2021-12-28

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Abstract

The invention discloses a loaded multifunctional catalysis composite material, a preparation method thereof and an application of the composite material to catalytic removal of water pollutants. The preparation method includes the steps: preparing a zinc oxide nano-sheet loaded nickel foam (Ni@ZnO) composite material by an electro-deposition method; compounding molybdenum disulfide micro-nano particles on ZnO porous nano-sheets by an electro-deposition method to obtain Ni@ZnO/MoS.sub.2. The composite material Ni@ZnO/MoS.sub.2 combines the advantages of components such as nickel foam, the zinc oxide nano-sheets and molybdenum disulfide from the point of material performances, high catalytic degradation activity and recycled performances are achieved, photo-catalysis and electro-catalysis are combined from the point of material application, and the catalytic activity of the composite material is improved by the aid of synergistic effects of photo-catalysis and electro-catalysis.

Claims

1. A preparation method of a loaded multifunctional catalysis composite material, characterized in that comprising the following steps: 1) preparing a zinc oxide nanosheet-loaded nickel foam composite by a first electrodeposition method using a zinc-containing aqueous solution and foamed nickel as raw materials; and 2) preparing a loaded multifunctional catalysis composite material by a second electrodeposition method using a sulphur-containing molybdenum compound aqueous solution and said zinc oxide nanosheet-loaded nickel foam composite as raw materials, wherein: in the step (1), zinc formate and zinc nitrate hexahydrate are added to water to obtain the zinc-containing aqueous solution; in the first electrodeposition method, nickel foam is used as a working electrode, platinum wire is used as a counter electrode, and a calomel electrode is a reference electrode, and the temperature of the zinc-containing aqueous solution is 25-85° C.; the first electrodeposition method is, first, deposited at −1.3 V for 10 s, and then deposited at −1.0 to −0.8 V for 100-300 s; after the first electrodeposition is completed, the zinc-containing foamed nickel is dried, and then treating at 350 to 500° C. for 1 to 2 hours under nitrogen protection, to obtain the zinc oxide nanosheet-loaded nickel foam composite material; and in the step (2), a thio-containing molybdenum compound and an inorganic salt are added to water to obtain the sulphur-containing molybdenum compound aqueous solution; in the second electrodeposition method, a zinc oxide nanosheet-supported nickel foam composite material is used as a working electrode, and the platinum wire is used as a counter electrode, calomel electrode is a reference electrode, the temperature of the sulphur-containing molybdenum compound aqueous solution is 25-85° C.; the second electrodeposition method is, first, deposited at −1.3 V for 10 s, and then deposited at −0.8˜−1.0 V for 100-300 s; after the second electrodeposition is completed, the molybdenum-containing zinc oxide nanosheet-loaded nickel foam composite is dried and then treated at 500-600° C. for 1 to 2 h under nitrogen protection to obtain a loaded multi-functional catalytic composite by electrodeposition.

2. The preparation method of a loaded multifunctional catalysis composite material according to claim 1, wherein the molar ratio of zinc formate to zinc nitrate hexahydrate is 1; the thiomolybdenum compound is tetrathiomolybdate, the inorganic salt is potassium chloride or sodium sulfate; the molar ratio of the tetrathiomolybdate to the inorganic salt is (0.1 to 1):1.

3. A catalytic removal method for water pollutants, characterized in that comprising the following steps: 1) preparing a zinc oxide nanosheet-loaded nickel foam composite by a first electrodeposition method using a zinc-containing aqueous solution and foamed nickel as raw materials; 2) preparing a loaded multifunctional catalysis composite material by a second electrodeposition method using a sulphur-containing molybdenum compound aqueous solution and said zinc oxide nanosheet-loaded nickel foam composite as raw materials; and 3) the loaded multifunctional catalysis composite material is added to the pollutant-containing water, and the catalytic removal of the organic pollutants is completed under electrification and/or light irradiation condition, wherein: in the step (1), zinc formate and zinc nitrate hexahydrate are added to water to obtain the zinc-containing aqueous solution; in the first electrodeposition method, nickel foam is used as a working electrode, platinum wire is used as a counter electrode, and a calomel electrode is a reference electrode, and the temperature of the zinc-containing aqueous solution is 25-85° C.; the first electrodeposition method is, first, deposited at −1.3 V for 10 s, and then deposited at −1.0 to −0.8 V for 100-300 s; after the first electrodeposition is completed, the zinc-containing foamed nickel is dried, and then treating at 350 to 500° C. for 1 to 2 hours under nitrogen protection, to obtain the zinc oxide nanosheet-loaded nickel foam composite material; and in the step (2), a thio-containing molybdenum compound and an inorganic salt are added to water to obtain a sulphur-containing molybdenum compound aqueous solution; in the second electrodeposition method, a zinc oxide nanosheet-supported nickel foam composite material is used as a working electrode, and the platinum wire is used as a counter electrode, calomel electrode is a reference electrode, the solution temperature of the sulphur-containing molybdenum compound aqueous solution is 25-85° C.; the second electrodeposition method is, first, deposited at −1.3 V for 10 s, and then deposited at −0.8˜−1.0 V for 100-300 s; after the second electrodeposition is completed, the molybdenum-containing zinc oxide nanosheet-loaded nickel foam composite is dried and then treated at 500-600° C. for 1 to 2 h under nitrogen protection to obtain a loaded multi-functional catalytic composite by electrodeposition.

4. The catalytic removal method for water pollutants according to claim 3, wherein the thiomolybdenum compound is tetrathiomolybdate, the inorganic salt is potassium chloride or sodium sulfate; the molar ratio of the tetrathiomolybdate to the inorganic salt is (0.1 to 1):1.

5. The catalytic removal method for water pollutants according to claim 3, wherein in the step (3), the illumination is 300 W xenon cold light source illumination, and the voltage applied is 0.4 V; the pollutant is an organic pollutant.

6. A loaded multifunctional catalysis composite material prepared by the preparation method of a loaded multifunctional catalysis composite material according to claim 1.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is the SEM image of ZnO nanosheets immobilized on Ni foam (Ni@ZnO) in implementation 1.

(2) FIG. 2 is the SEM image of MoS.sub.2 immobilized on Ni@ZnO (Ni@ZnO/MoS.sub.2) in implementation 2.

(3) FIG. 3 shows the photoelectrocatalytic degradation patterns (a) of acid red 1 over Ni@ZnO/MoS.sub.2 in implementation 6.

(4) FIG. 4 shows the recycle of the Ni@ZnO/MoS.sub.2 for degradation of acid red 1 in implementation 7.

DETAILED DESCRIPTION OF THE INVENTION

(5) The invention will be made a further explanation according to the following figures and the specific implementations.

(6) Implementation 1:

(7) Synthesis of ZnO nanosheets immobilized on Ni foam (Ni@ZnO)

(8) At room temperature, 5 mM zinc formate and 5 mM zinc nitrate hexahydrate were first dissolved in 100 ml of an aqueous solution to prepare an electrolyte solution. Nickel foam is used as the working electrode, platinum wire is used as the counter electrode, and the calomel electrode is used as the reference electrode to connect the circuit. Electrodeposition experiments were carried out under an electrochemical workstation. First, an external bias voltage of −1.3 V was set and electrodeposited for 10 s, then a bias voltage of −1.0 V was set and deposited for 300 s. The sample was taken out from the working electrode and dried under vacuum at 60° C. for 12 h. After being placed at 350° C. (the temperature is 2° C./min), the temperature is 1 h under nitrogen protection. Finally, the obtained nickel foam composite is a zinc oxide nanosheet-loaded nickel foam composite (Ni@ZnO). As can be seen from FIG. 1, the ZnO nanosheets are porous nanosheets and are uniformly distributed on the surface of the nickel foam.

(9) Implementation 2:

(10) Preparation of molybdenum disulfide micro-nanoparticle composite zinc oxide nanosheet-supported nickel foam composite (Ni@ZnO/MoS.sub.2): first dissolve 0.05 mol of tetrathiomolybdate and 0.1 mol of potassium chloride in 100 ml aqueous solution at room temperature, to obtain an electrolyte solution. Ni@ZnO is used as the working electrode, the platinum wire electrode is the counter electrode, and the calomel electrode is used as the reference electrode. After the connection, it is operated on the electrochemical workstation, first deposited for 10 s when the applied bias voltage is −1.3 V, and then at an applied bias of −1.0 V and deposited for 100 s, the sample is taken out from the working electrode and vacuum dried at 60° C. for 12 h. After being placed at 600° C. (the heating rate is 5° C./min), the temperature is kept for 2 hours under nitrogen protection. Finally, the obtained nickel foam composite material is molybdenum disulfide micro-nanoparticle composite zinc oxide nanosheet-loaded nickel foam composite (Ni@ZnO/MoS.sub.2). As can be seen from FIG. 2, the MoS.sub.2 micro/nanoparticles are uniformly distributed on the ZnO nanosheets.

(11) Implementation 3:

(12) Photocatalytic Degradation of acid red 1 by Ni@ZnO

(13) Taking 1*4 cm.sup.2 of Ni@ZnO into 100 mL of acid red 1 solution with a concentration of 20 mg/mL, In the process of photocatalytic degradation, the solution was added 300 W Xenon lamp cold light source with stirring for 1 h, the concentration of the solution was measured at a wavelength of 530 nm by an UV-visible spectrophotometer, and calculate the corresponding acid red in water sample according to the standard working curve. 1 residual concentration. After the test, Ni@ZnO photocatalytic degraded 7% of the above acid red 1 solution after 1 h. The removal rate was 7%. The above results show that under visible light irradiation, the photocatalytic performance of Ni@ZnO is weak, which is mainly due to the wide bandgap of ZnO photocatalyst. The spectral absorption range of the ZnO photocatalyst is mainly in the ultraviolet region and there is little absorption in the visible region.

(14) Implementation 4:

(15) Photocatalytic Degradation of acid red 1 by Ni@ZnO/MoS.sub.2

(16) Taking 1*4 cm.sup.2 of Ni@ZnO/MoS.sub.2 into 100 mL of acid red 1 solution with a concentration of 20 mg/mL, In the process of photocatalytic degradation, the solution was added 300 W Xenon lamp cold light source with stirring for 1 h, the concentration of the solution was measured at a wavelength of 530 nm by an UV-visible spectrophotometer, and calculate the corresponding acid red in water sample according to the standard working curve residual concentration. The experimental results show that Ni@ZnO/MoS.sub.2 photocatalytic degrades 34% of the acid red 1 solution after 1 h, which is compared with the photocatalytic performance of Ni@ZnO in implementation 3, the photocatalytic properties of the composite material is greatly improved after loading MoS.sub.2.

(17) Implementation 5:

(18) Electcatalytic Degradation of acid red 1 by Ni@ZnO/MoS.sub.2

(19) Electrocatalytic experiments were performed on a three-electrode electrochemical station. 1*4 cm.sup.2 of Ni@ZnO/MoS.sub.2 was used as working electrode, platinum wire electrode was used as the counter electrode and saturated calomel electrode was the reference electrode. Configuring 100 ml of acid red 1 (20 mg/L) containing 0.05 mol of sodium sulfate as the electrolyte solution. After the electrode was installed, an externally biased 0.4 V was applied for 40 minutes. The concentration of the solution was measured at a wavelength of 530 nm by an UV-visible spectrophotometer, and calculate the corresponding acid red in water sample according to the standard working curve residual concentration.

(20) Implementation 6:

(21) Photoelectrochemical Degradation of acid red 1 by Ni@ZnO/MoS.sub.2

(22) Ni@ZnO/MoS.sub.2 obtained in Implementation 2 of 1*4 cm.sup.2 was weighed and placed in 100 ml of acid red 1 aqueous solution with a concentration of 20 mg/l. 0.71 g of sodium sulfate was added and configured as an electrolyte solution. Ni@ZnO/MoS.sub.2 was used as the working electrode, the platinum wire electrode was used as the counter electrode, and the calomel electrode was used as the reference electrode. The electrode was connected and used. First, in the dark, let stand for 30 minutes, then open a 300 W xenon cold light source for irradiation, and use the electrochemical workstation to test the electrolytic solution bias voltage of 0.4 V for photoelectrocatalytic degradation experiments. A sample of 3 ml was taken every 10 minutes, and the absorbance of the water sample at a wavelength of 530 nm was measured by an ultraviolet-visible spectrophotometer, and the residual concentration of acid red 1 in the corresponding water sample was calculated in combination with a standard working curve. FIG. 3 is a graph showing the relationship between the residual rate of acid red 1 and the time in a water sample during a 40 W xenon cold light source irradiation and a 0.4 V bias for 40 min. It can be seen from FIG. 3 that the concentration of the contaminant changes little after 30 minutes of protection from light, and in the process of photoelectrocatalysis, the electron and the space are effectively effective due to the simultaneous illumination and the applied bias. The separation of the holes, thereby improving the catalytic performance, can completely degrade all of the acid red 1 after 40 minutes of catalysis.

(23) Implementation 7:

(24) Recycled photoelectrochemical degradation of acid red 1 by Ni@ZnO/MoS.sub.2

(25) The stability and reusability performance of Ni@ZnO/MoS.sub.2 was tested by photoelectrocatalytic experiment, in which the condition was keep by above-mentioned test. In detail, Ni@ZnO/MoS.sub.2 was taken out by tweezers and dried for next degradation experiment. The dye solution was the 100 ml of acid red 1 (20 mg/L). In detail, 1*4 cm.sup.2 of Ni@ZnO/MoS.sub.2 from implementation 2 were used as the working electrode, and the platinum wire electrode was used as the counter electrode. The saturated calomel electrode is a reference electrode. Configuring 100 ml of acid red 1 (20 mg/L) containing 0.05 mol of sodium sulfate as the electrolyte solution. After the electrode was installed, an external bias voltage of 0.4 V was applied, and the working electrode was irradiated with light for 40 minutes, and the concentration of the test solution was sampled every 10 minutes. The concentration of the solution was measured at a wavelength of 530 nm by an UV-visible spectrophotometer, and calculate the corresponding acid red in water sample according to the standard working curve residual concentration.

(26) In FIG. 4, the photoelectrocatalytic degradation experiment in implementation 6 is repeated and totally reused for five times. As shown in FIG. 4, Ni@ZnO/MoS.sub.2 has stable catalytic performance after the fifth cycle catalytic experiments. It demonstrated that Ni@ZnO/MoS.sub.2 has good stability. In the recycling process, the composite material can be taken out easily from the solution by tweezers, which is much more convenient than nanoparticles in practical application.

(27) When using the catalyst of the invention to remove the pollutants from water, a bias voltage is applied as well as under the light irradiation. Biased voltage can force the directional movement of photo-generated electrons, greatly accelerate the separation of photo-generated electrons and holes. Therefore, this photoelectrocatalytic degradation technology (electric field assisted photocatalysis) will have more application prospects.