PREPARATION OF THREE-DIMENSIONAL MAGNETIC GAMMA MANGANESE DIOXIDE/ZINC IRON OXIDE NANOHYBRID ON GRAPHENE, AND USE THEREOF AS CATALYST FOR DECOMPOSING HARMFUL ORGANIC WASTE
20220193641 · 2022-06-23
Assignee
Inventors
Cpc classification
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
B82Y25/00
PERFORMING OPERATIONS; TRANSPORTING
H01F1/42
ELECTRICITY
B01J21/10
PERFORMING OPERATIONS; TRANSPORTING
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J21/10
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A nanohybrid includes: reduced graphene oxide (rGO); zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles dispersed in the rGO; and manganese dioxide (MnO.sub.2) nanoflakes three-dimensionally attached on the rGO. The nanohybrid reduces recombination of graphene through the synergistic effects of MnO.sub.2 nanoflakes, ZnFe.sub.2O.sub.4 nanoparticles, and graphene, and increases the surface area of the catalyst, thus being capable of exhibiting higher catalytic activity than the conventional δ-MnO.sub.2@ZnFe.sub.2O.sub.4, γ-MnO.sub.2@rGO, and ZnFe.sub.2O.sub.4@rGO composites in the decomposition of harmful organic waste.
Claims
1. A three-dimensional (3D) MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst comprising: reduced graphene oxide (rGO); zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles dispersed in the rGO; and manganese dioxide (MnO.sub.2) nanoflakes attached three-dimensionally on the rGO.
2. The 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst according to claim 1, wherein the manganese dioxide (MnO.sub.2) is in the gamma (γ) form.
3. The 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst according to claim 1, wherein an average thickness of the manganese dioxide (MnO.sub.2) nanoflakes is 2 to 5 nm.
4. The 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst according to claim 1, wherein the MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid has a Brunauer-Emmett-Teller (BET) specific surface area of 200 to 500 m.sup.2/g and includes pores with an average diameter of 2 to 15 nm.
5. A catalyst for decomposing harmful organic waste comprising the 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst according to claim 1 and peroxymonosulfate (PMS).
6. A method for preparing a three-dimensional (3D) MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst, comprising: dispersing zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles in a graphene oxide (GO) solution to prepare a ZnFe.sub.2O.sub.4/GO solution; adding a manganese precursor and an acid to the ZnFe.sub.2O.sub.4/GO solution to prepare a suspension; and performing heat treatment of the suspension to obtain a nanohybrid (MnO.sub.2@ZnFe.sub.2O.sub.4/rGO) with manganese dioxide (MnO.sub.2) nanoflakes attached three-dimensionally on reduced graphene oxide (rGO) in which the zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles are dispersed.
7. The method according to claim 6, wherein the manganese precursor is any one selected from the group consisting of potassium permanganate (KMnO.sub.4), manganese nitrate (Mn(NO.sub.3).sub.2), manganese hydrochloride (MnCl.sub.2), manganese sulfate (MnSO.sub.4), and manganese acetate (Mn(CH.sub.3COO).sub.2).
8. The method according to claim 6, wherein the acid is any one selected from the group consisting of hydrochloric acid (HCl), sulfuric acid (H.sub.2SO.sub.4), and nitric acid (HNO.sub.3).
9. The method according to claim 6, wherein 0.1 to 0.7 g of the manganese precursor is included, and 0.3 to 2.0 mL of the acid is included.
10. The method according to claim 6, wherein the heat treatment of the suspension is carried out at 50 to 150° C. for 5 to 20 hours.
11. The method according to claim 6, wherein an average thickness of the manganese dioxide (MnO.sub.2) nanoflakes is 2 to 5 nm.
12. The method according to claim 6, wherein the MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid has a BET specific surface area of 200 to 500 m.sup.2/g and includes pores with an average diameter of 2 to 15 nm.
Description
BRIEF DESCRIPTIONS OF DRAWINGS
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MODES FOR CARRYING OUT INVENTION
[0024] Hereinafter, the present invention will be described in detail.
[0025] The present inventors prepared a 3D γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst using a simple hydrothermal method and have completed the present invention by determining that it can exhibit high catalytic activity in degrading harmful wastewater compared to the existing δ-MnO.sub.2@ZnFe.sub.2O.sub.4, γ-MnO.sub.2@rGO, and ZnFe.sub.2O.sub.4@rGO composites by reducing aggregation of graphene through the synergetic effects of MnO.sub.2 nanoflakes, ZnFe.sub.2O.sub.4 nanoparticles, and graphene, and increasing activity of a radical source by increasing the surface area of the catalyst.
[0026] The present invention provides a 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst containing reduced graphene oxide (rGO); zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles dispersed in the rGO; and manganese dioxide (MnO.sub.2) nanoflakes attached three-dimensionally on the rGO.
[0027] Here, the manganese dioxide (MnO.sub.2) may have the gamma (γ) form, and an average thickness of the prepared manganese dioxide (MnO.sub.2) nanoflakes may be 2 to 5 nm.
[0028] In addition, the MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid can increase the Brunauer-Emmett-Teller (BET) specific surface area to 200 to 500 m.sup.2 g.sup.−1 by including pores with an average diameter of 2 to 15 nm, thus increasing the catalytic activity for degrading harmful organic waste.
[0029] Further, the present invention provides a catalyst for decomposing harmful organic waste, containing the 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst and peroxymonosulfate (PMS).
[0030] Here, a high-efficiency catalytic effect can be exhibited through the high surface area of the 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst and sulfate radicals generated by activation of PMS by MnO.sub.2 and ZnFe.sub.2O.sub.4. Particularly, in the case that 0.2 g L.sup.−1 δ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid and 2.0 g L.sup.−1 PMS are added, harmful organic waste can be completely degraded within a short time.
[0031] Further, the present invention provides a 3D MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid catalyst preparation method including dispersing zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles in a graphene oxide (GO) solution to prepare a ZnFe.sub.2O.sub.4/GO solution; adding a manganese precursor and an acid to the ZnFe.sub.2O.sub.4/GO solution to prepare a suspension; and performing heat treatment of the suspension to obtain a nanohybrid (MnO.sub.2@ZnFe.sub.2O.sub.4/rGO) with manganese dioxide (MnO.sub.2) nanoflakes attached three-dimensionally on reduced graphene oxide (rGO) in which zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles are dispersed.
[0032] Here, the manganese precursor may be any one selected from the group consisting of potassium permanganate (KMnO.sub.4), manganese nitrate (Mn(NO.sub.3).sub.2), manganese hydrochloride (MnCl.sub.2), manganese sulfate (MnSO.sub.4), and manganese acetate (Mn(CH.sub.3COO).sub.2), but is not limited thereto.
[0033] In addition, the acid may be any one selected from the group consisting of hydrochloric acid (HCl), sulfuric acid (H.sub.2SO.sub.4), and nitric acid (HNO.sub.3), but is not limited thereto.
[0034] In addition, 0.1 to 0.7 g of the manganese precursor may be included, and 0.3 to 2.0 mL of the acid may be included. Preferably, 0.45 g of the manganese precursor and 1 mL of the acid may be included.
[0035] In addition, the heat treatment of the suspension may be performed at 50 to 150° C. for 5 to 20 hours, and preferably, at 100° C. for 12 hours, but is not limited thereto.
[0036] Here, in the case of exceeding the conditions of the preparation method, the nanohybrid (MnO.sub.2@ZnFe.sub.2O.sub.4/rGO) with manganese dioxide (MnO.sub.2) nanoflakes attached three dimensionally on reduced graphene oxide (rGO) in which zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles are dispersed according to the present invention is not formed properly, so the catalytic activity is not excellent, which may cause a problem that it cannot be usefully used as a catalyst for decomposing harmful organic waste.
[0037] In addition, an average thickness of the prepared manganese dioxide (MnO.sub.2) nanoflakes may be 2 to 5 nm, and the MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid may include pores having an average diameter of 2 to 15 nm to increase the BET specific surface area to 200 to 500 m.sup.2/g, thereby increasing the catalytic activity for decomposing harmful organic waste.
[0038] According to the present invention, the nanohybrid (MnO.sub.2@ZnFe.sub.2O.sub.4/rGO) with manganese dioxide (MnO.sub.2) nanoflakes attached three-dimensionally on reduced graphene oxide (rGO) in which zinc ferrite (ZnFe.sub.2O.sub.4) nanoparticles are dispersed was prepared simply using the hydrothermal self-assembly synthesis method. This nanohybrid exhibited a high BET specific surface area which is an important property for excellent catalytic activity, through the synergistic effects of MnO.sub.2, ZnFe.sub.2O.sub.4, and graphene. Further, it exhibited a high-efficiency catalytic effect through the sulfate radicals (SO.sub.4*) generated by the activation of PMS by MnO.sub.2 and ZnFe.sub.2O.sub.4, could be recovered easily using a magnet, and could be reused more than 5 times. Therefore, since the nanohybrid catalyst according to the present invention has excellent catalytic activity and reusability, it may be usefully applied to removal of hard-to-degrade waste materials.
[0039] Hereinafter, the present invention will be described in detail through examples. It would be clear to a person skilled in the art that these examples are merely for illustrating the present invention specifically and that the scope of the present invention is not limited by the examples.
<Example 1>Preparation of 3D δ-MnO.SUB.2.@ZnFe.SUB.2.O.SUB.4./rGO Nanohybrid Catalyst
[0040] All materials used below were of high purity grade, purchased from Sigma-Aldrich, and used as received without further purification. Graphene oxide (GO) was generated using Tour's method (ACS Nano, 4 (2010) 4806-4814; 12 (2018) 2078).
<Comparative Example 1>Preparation of δ-MnO.SUB.2.@ZnFe.SUB.2.O.SUB.4 .Catalyst
[0041] A catalyst was prepared using the same process described above for Example 1 except that GO was not included (hereinafter, referred to as ‘δ-MnO.sub.2@ZnFe.sub.2O.sub.4’).
<Comparative Example 2>Preparation of γ-MnO.SUB.2.@rGO Catalyst
[0042] A catalyst was prepared using the same process described above for Example 1 except that ZnFe.sub.2O.sub.4 was not included (hereinafter, referred to as ‘γ-MnO.sub.2@rGO’).
<Comparative Example 3>Preparation of ZnFe.SUB.2.O.SUB.4.@rGO Catalyst
[0043] A catalyst was prepared using the same process described above for Example 1 except that MnO.sub.2 was not included (hereinafter, referred to as ‘ZnFe.sub.2O.sub.4@rGO’).
<Example 2>Analysis
[0044] Powder X-ray diffraction (XRD; PANalytical, X′Pert-PRO MPD) was carried out using Cu Kα radiation. The structural information of the samples was analyzed using Fourier-transform infrared (FT-IR; Bio-Rad, Excalibur Series FTS 3000) spectroscopy and Raman spectroscopy (Horiba, XploRA plus). X-ray photoelectron spectroscopy (XPS; Kratos Analytical, AXIS Nova) was used to examine the surface components of the samples. The Brunauer-Emmett-Teller (BET) specific surface area (S.sub.BET) and pore size distribution (PSD) of the samples were investigated using an N.sub.2 adsorption-desorption apparatus (Micromeritics 3Flex Surface Characterization Analyzer). Field-emission scanning electron microscopy (FE-SEM; Hitachi, S-4800) and transmission electron microscopy (TEM; Philips, CM 200) were used to determine the morphology and structure of the samples. Magnetization measurements were carried out at room temperature using a vibrating sample magnetometer (VSM; Dexing, Model 250). The metal content of the composite was analyzed by inductively coupled plasma atomic emission spectroscopy (ICP-AES; PerkinElmer, Optima 8300).
<Example 3>Catalytic Activity Measurement
[0045] In a catalytic activity measurement test, a 10 mg of catalyst was added to 50 mL of 20 ppm phenol solution, which was then stirred for 30 minutes to achieve adsorption-desorption equilibrium. Then, to start reaction tests, 0.3 mM peroxymonosulfate (PMS) was added to the reaction solution. After a certain period of time, 1.5 mL of the aqueous sample was withdrawn using a syringe and filtered into a vial. The concentration of phenol was analyzed by high-performance liquid chromatography (HPLC; Young Lin, Series YL9100) equipped with a YL9120 UV/Vis detector; the UV wavelength was adjusted to 275 nm. A C-18 column (Sun Fire) was used to separate the organic solution from a mobile solution at a flow rate of 1 mL min.sup.−1. The eluent was prepared by mixing water, 1 vol. % acetic acid solution, and methanol in the ratio of 50:40:10. To examine catalytic stability and reusability, the nanohybrid was used 5 times. After each experiment, it was collected using a magnet, washed with deionized water, and dried in a vacuum oven at room temperature.
<Experimental Example 1>Structural Analysis of 3D γ-MnO.SUB.2.@ZnFe.SUB.2.O.SUB.4./rGO Nanohybrid
[0046] 1. XRD Analysis
[0047] XRD analysis was performed on ZnFe.sub.2O.sub.4 and the composites of Example 1 and Comparative Examples 1 to 3 to determine the crystalline structure of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid (
[0048] 2. SEM, TEM Analysis
[0049]
[0050] The HRTEM image in
[0051] Based on the experimental results, a possible mechanism was proposed to understand growth mechanism of MnO.sub.2 nanoflakes on rGO sheets (
[0052] 3. XPS Analysis
[0053] The chemical bonding state of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid was analyzed by XPS (
[0054] 4. Raman Spectrum Analysis
[0055]
[0056] 5. FT-IR Analysis
[0057] Evidence for the reduction of oxygen functional groups on the GO surface was obtained from the FT-IR spectra of GO and γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid, as shown in
[0058] 6. S.sub.BET, PSD Analysis
[0059] As shown in
TABLE-US-00001 TABLE 1 Pore Average pore First order S.sub.BET Volume diameter rate constant Sample (m.sup.2 g.sup.−1) (cm.sup.3 g.sup.−1) (nm) (min.sup.−1) R.sup.2 γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO 376.9 1.055 8.15 0.094 0.9912 δ-MnO.sub.2@ZnFe.sub.2O.sub.4 223.0 0.942 16.66 0.033 0.972 γ-MnO.sub.2@rGO 46.0 0.246 24.98 0.0235 0.988 ZnFe.sub.2O.sub.4@rGO 153.9 0.339 8.13 0.0114 0.983
<Experimental Example 2>Catalytic Activity
[0060] 1. Catalytic Activity of γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO Nanohybrid
[0061] The catalytic performance of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid and the other composites for phenol degradation via peroxymonosulfate (PMS) activation was analyzed (FIG. 9a). Control experiments for catalytic activity using PMS only and γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid without PMS were conducted. As a result, the sample using the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid and PMS showed the highest catalytic efficiency among all the samples tested. Further, in the absence of a catalyst, PMS could not be activated and the amount of sulfate radicals (SO.sub.4′.sup.−) generated was insufficient to degrade the 20 ppm phenol solution. Furthermore, the use of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid without the addition of PMS resulted in the adsorption of approximately 20% of phenol after 3 hours. By combining PMS with the composites, PMS was activated on the active sites of the metal oxides, and the catalytic activity of the composites was observed in the following order: γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO >δ-MnO.sub.2@ZnFe.sub.2O.sub.4 >γ-MnO.sub.2@rGO >ZnFe.sub.2O.sub.4@rGO.
[0062] In particular, the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid showed complete degradation of 20 mg L.sup._(20 ppm) phenol after 30 min in the presence of PMS. A comparison with the results of the other composites revealed 22, 39, and 41% phenol degradation on ZnFe.sub.2O.sub.4@rGO, γ-MnO.sub.2@rGO, and δ-MnO.sub.2@ZnFe.sub.2O.sub.4, respectively, indicating the synergetic effects on catalytic activity of combining MnO.sub.2, ZnFe.sub.2O.sub.4, and rGO into a nanohybrid. This high-efficiency catalytic effect is attributed to the high surface area of the nanohybrid compared to the other composites (Table 1) and the ability of both MnO.sub.2 and ZnFe.sub.2O.sub.4 to activate PMS through an electron transfer mechanism to produce sulfate radicals (Eqs. (1) to (4) below). As a result, the composites containing both MnO.sub.2 and ZnFe.sub.2O.sub.4 showed high catalytic efficiency compared to other composites lacking one of them (
[0063] Further analysis of the performance of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid under different reaction conditions was carried out and the effects of catalyst loading and PMS loading were analyzed (
[0064] 2. Magnetism and Reusability of γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO Nanohybrid Catalyst
[0065] The catalyst magnetism and reusability of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid were evaluated from successive catalytic experiments by taking advantage of the magnetic property of the nanohybrid, which exhibited paramagnetic behavior and a slim hysteresis loop with a saturation magnetization value of approximately 7 emu g.sup.−1 at 2 θ,000 Oe, magnetic coercivity (Hc) of 293.67 Oe, and remanence (M.sub.R) of 0.266 emu g.sup.−1 (
[0066] 3. Catalytic Mechanism of γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO Nanohybrids
[0067] Based on the above results, an activation mechanism of peroxymonosulfate (PMS) on the active sites of the γ-MnO.sub.2@ZnFe.sub.2O.sub.4/rGO nanohybrid for phenol degradation is as follows (Eqs. (1) to (7) and
[0068] [Equations]
Mn(IV)+HSO.sub.5.sup.−.fwdarw.Mn(III)+HO*+SO.sub.4*.sup.− (1)
Mn(III)+HSO.sub.5.sup.−.fwdarw.Mn(IV)+SO.sub.5*.sup.−+H.sup.+ (2)
Fe(II)+HSO.sub.5.sup.−.fwdarw.Fe(III)+SO.sub.4*.sup.−+OH.sup.− (3)
Fe(III)+HSO.sub.5.sup.−.fwdarw.Fe(II)+SO.sub.5*.sup.−−+H.sup.+ (4)
2SO.sub.5*.sup.−+2OH.sup.−.fwdarw.2SO.sub.4.sup.2−+2HO*+O.sub.2 (5)
Fe(III)+Mn(III).fwdarw.Fe(II)+Mn(IV) (6)
SO.sub.4*.sup.−+HO*+C.sub.6H.sub.6OH.fwdarw.Several steps.fwdarw.CO.sub.2+H.sub.2O+SO.sub.4.sup.2− (7)
[0069] The Mn(IV)/Mn(III) and Fe(II)/Fe(III) transitions involve electron transfer, which is responsible for the catalytic reaction. In the first stage, the active sites of both MnO.sub.2 and ZnFe.sub.2O.sub.4 on the nanohybrid can activate PMS to generate active radicals (Eqs. (1) to (4)), which can contribute to phenol degradation (Eq. (7)). Hydroxyl radicals (HO) are generated further after the depletion of SO.sub.4*.sup.− in a rapid reaction with phenol in the first stage (Eq. (5)), and HO* becomes the only radical that reacts with phenol in the last stage of the reaction. The return to the original oxidation states of the metals (Mn(IV) and Fe(II)) is due to the recovery reactions on the reduced hybrid (Eq. (6)).