Copper-doped iron metal-organic framework, preparation method thereof, and application method for activation of persulfate to treat organic wastewater

Abstract

The present invention discloses a copper-doped iron metal-organic framework, a preparation method thereof, and an application method for activation of persulfate to treat organic wastewater. The copper-doped iron metal-organic framework is prepared by solution impregnation method, using relatively large specific surface area and more hollow structures of the iron metal-organic framework to effectively load copper ion. This method uses the unsaturated-coordinate iron active center on the iron metal-organic framework and copper ions on the load as a catalyst body, utilizing catalytic synergies of both to efficiently and continuously activate persulfate to produce sulfate radical anion for degradation of organic pollutants. This method is suitable for various organic wastewater, with high catalytic activity, good durability, easy operation and easy recovery, and activation effect of this heterogeneous catalyst is still high even after being used repeatedly, having a great application prospect in degradation of organic pollutants in water.

Claims

1. A preparation method of copper-doped iron metal-organic framework, characterized in that, steps are as follows: (1) preparation of iron metal-organic framework: dissolving 0.1350.675 g FeCl.sub.3.6H.sub.2O in 525 mL N,N-Dimethylformamide, and adding 0.0410.206 g 1,4-benzenedicarboxylic acid, to obtain a mixture solution, stirring the mixture solution until completely dissolved, then transferring the mixture solution into a 20100 mL fluoropolymer-lined high-pressure reactor, putting the high-pressure reactor into a thermostatic blast drying oven for reaction; (2) after cooling the high-pressure reactor to room temperature, high-speed centrifuging the reaction solution at a speed of 800010000 r to obtain a yellow solid, successively washing the yellow solid with absolute ethyl alcohol, then putting the yellow solid into a vacuum drying oven for drying, to obtain an iron metal-organic framework, labeled as MIL-101(Fe); (3) preparation of copper-doped iron metal-organic framework: successively weighing Cu(NO.sub.3).sub.2.3H.sub.2O and citric acid and dissolving them in 100 mL deionized water to obtain a solution, then adding 0.20.4 g of the MIL-101(Fe) prepared in step (2) into the solution to obtain a mixture, uniformly mixing the mixture by a magnetic stirrer, then transferring the mixture into the fluoroplymer-lined high-pressure reactor, putting the high-pressure reactor into the thermostatic blast drying oven for reaction; (4) after cooling the high-pressure reactor to room temperature, high-speed centrifuging the reaction solution at a speed of 800010000 r to obtain a solid, repeatedly washing the solid with deionized water, until no blue color is found in washing liquid; (5) processing the material obtained in step (4) in a temperature programming tube furnace, with specific operation being: heating the tube furnace rapidly to 200280 C. in 25 minutes35 minutes, high-temperature processing the material under the atmosphere of nitrogen; (6) after cooling the tube furnace to room temperature, taking out the material, with the material being copper-doped iron metal-organic framework, labeled as Cu/MIL-101(Fe), then storing the Cu/MIL-101(Fe) in a dryer.

2. The preparation method of copper-doped iron metal-organic framework according to claim 1, wherein the reaction mentioned in step (1) is performed at a temperature of 110 C., with a reaction time being 24 hours.

3. The preparation method of copper-doped iron metal-organic framework according to claim 1, wherein washing the solid mentioned in step (2) is performed for 2 times, 3 hours per wash; the drying in the vacuum drying oven is performed at a temperature of 150 C., for 12 hours; and the high-temperature processing mentioned in step (5) is performed for 4 hours.

4. The preparation method of copper-doped iron metal-organic framework according to claim 1, wherein Cu.sup.2+ in the Cu(NO.sub.3).sub.2.3H.sub.2O and the MIL-101(Fe) mentioned in step (3) have a mass ratio of 4%, 6%, 8% or 10%; the amount of citric acid is 0.036 g0.18 g; the stirring is performed for 4 hours; the high-pressure reactor has a volume of 100 mL; and the reaction is performed for 8 hours at 80 C.

5. A copper-doped iron metal-organic framework prepared by the preparation method according to claim 1.

6. A copper-doped iron metal-organic framework prepared by the preparation method according to claim 2.

7. A copper-doped iron metal-organic framework prepared by the preparation method according to claim 3.

8. A copper-doped iron metal-organic framework prepared by the preparation method according to claim 4.

9. An application method of the copper-doped iron metal-organic framework according to claim 5 for activation of persulfate to treat organic wastewater, characterized in that, steps are as follows: adding copper-doped iron metal-organic framework catalyst and persulfate oxidant into the organic wastewater simultaneously, then shaking in a shaker, reacting for 10 minutes240 minutes at room temperature.

10. The application method of the copper-doped iron metal-organic framework for activation of persulfate to treat organic wastewater according to claim 9, wherein the persulfate is sodium persulfate or potassium persulfate.

11. The application method of the copper-doped iron metal-organic framework for activation of persulfate to treat organic wastewater according to claim 9, wherein a molar ratio between the persulfate oxidant and organic pollutants is (80140):1.

12. The application method of the copper-doped iron metal-organic framework for activation of persulfate to treat organic wastewater according to claim 9, wherein a dosing quantity of the copper-doped iron metal-organic framework catalyst is 0.10.6 g/L.

13. The application method of the copper-doped iron metal-organic framework for activation of persulfate to treat organic wastewater according to claim 9, wherein the shaker has a speed of 50-500 rpm.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is an X-ray crystal diffraction pattern of the iron metal-organic framework.

(2) FIG. 2 is an X-ray crystal diffraction pattern of the 6% copper-doped iron metal-organic framework.

(3) FIG. 3 is an X-ray crystal diffraction pattern of the 8% copper-doped iron metal-organic framework.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

(4) The present invention takes dyestuff wastewater as the typical organic wastewater. The dyestuff wastewater affects the visual appearance and contains the large amount of pollutants that are difficult to be biodegraded. Acid dye AO7 is chosen in the following several embodiments as a target pollutant. The present invention is further described below by embodiments, illustrating prominent characteristics and significant progress of the present invention, only intending to explain the present invention but not limit the present invention to the following examples.

(5) Embodiment 1

(6) The present embodiment compared a copper-doped iron metal-organic framework activating sodium persulfate, the copper-doped iron metal-organic framework used alone, an iron metal-organic framework used alone, and sodium persulfate used alone for removal rates of AO7.

(7) The copper-doped iron metal-organic framework: 0.675 g FeCl.sub.3.6H.sub.2O was dissolved in 25 mL N,N-Dimethylformamide (DMF), and 0.206 g 1,4-benzenedicarboxylic acid (BDC) was added, to obtain a mixture solution. The mixture solution was stirred until completely dissolved, then it was transferred into a 100 mL Teflon-lined high-pressure reactor, and then the high-pressure reactor was put into a thermostatic blast drying oven for reaction at 110 C. for 24 hours. After the high-pressure reactor was cooled to room temperature, the reaction solution was high-speed centrifuged at a speed of 8000 r to obtain a yellow solid. The solid was successively washed with absolute ethyl alcohol for 2 times, 3 hours per wash, and then it was put into a vacuum drying oven at 150 C. for drying for 12 hours, to obtain an iron metal-organic framework, labeled as MIL-101(Fe), with an X-ray crystal diffraction pattern being shown in FIG. 1. 0.076 g Cu(NO.sub.3).sub.2.3H.sub.2O and 0.09 g Citric acid were successively weighed and were dissolved in 100 mL deionized water to obtain a solution, and then 0.2 g MIL-101(Fe) was added into the solution to obtain a mixture. The mixture was uniformly mixed by a magnetic stirrer for 4 hours, and then the mixture was transferred into a 100 mL Teflon-lined high-pressure reactor. The high-pressure reactor was put into the thermostatic blast drying oven for reaction at 80 C. for 8 hours. After the high-pressure reactor was cooled to room temperature, the reaction solution was high-speed centrifuged at a speed of 8000 r to obtain a solid. The solid was repeatedly washed with deionized water, until no blue color was found in washing liquid. The above obtained material was processed in a temperature programming tube furnace, with specific operation being: the tube furnace was rapidly heated to 280 C. in 35 min, and the material was high-temperature processed for 4 hours under the atmosphere of nitrogen; after the tube furnace was cooled to room temperature, the material was taken out, with the material being copper-doped iron metal-organic framework, labeled as 10% Cu/MIL-101(Fe), and then it was stored in a dryer for later use.

(8) (1) In a heterogeneous reaction using the copper-doped iron metal-organic framework for activation of sodium persulfate, a conical flask was used as a reactor, and wastewater was 100 mL 0.1 mM/L AO7 solution. 0.02 g copper-doped iron metal-organic framework with copper doping content 10% as a catalyst and 0.1904 g sodium persulfate (molar ratio PS/AO7=80) as an oxidant were added into the reactor simultaneously, and then the conical flask was put into a shaker with a speed of 180 rpm at a temperature of 25 C.

(9) (2) Only the copper-doped iron metal-organic framework in the reaction system (1) was changed to iron metal-organic framework, and the other conditions were the same as the reaction system (1).

(10) (3) Without adding sodium persulfate, the copper-doped iron metal-organic framework was added alone, and the other conditions were the same as the reaction system (1).

(11) (4) Without adding sodium persulfate, the iron metal-organic framework was added alone, and the other conditions were the same as the reaction system (1).

(12) (5) Without adding any catalyst, sodium persulfate was added alone, and the other conditions were the same as the reaction system (1).

(13) The results of the five processes are shown in Table 1:

(14) TABLE-US-00001 TABLE 1 Removal Removal Removal Removal Removal Time rate rate rate rate rate min % (1) % (2) % (3) % (4) % (5) 0 0 0 0 0 0 10 4 20.1 0.4 4.7 0 20 8.4 26 0.7 5.2 0.2 30 12.6 32.4 0.8 6.3 0.3 60 17 34.2 1.1 7.4 0.6 90 25.6 38.4 1.4 7.7 0.6 120 30.8 41.5 1.6 8.4 0.7 180 59.7 47.8 1.7 9 0.8 210 83.8 53.7 1.9 9.5 0.8 240 95.2 59.5 2.5 12.6 1

(15) The results in Table 1 illustrate that either the catalyst or sodium persulfate alone has weak removal efficiency on AO7. When the catalyst and sodium persulfate were added simultaneously, however, the removal rate of AO7 is significantly increased. It is not difficult to find that in the system where sodium persulfate (0.1904 g) presents, the catalytic effect of the added copper-doped iron metal-organic framework is far superior to that of the iron metal-organic framework. For example, at 180 min, the former is 59.7% while the latter is 47.8%. At 240 min, the removal rate of the former is higher than 95%, while the latter is less than 60%.

(16) Embodiment 2

(17) The present embodiment compared sodium persulfate activated at different copper doping amounts (10%, 8%, 6%, 4%) for removal rates of AO7.

(18) The copper-doped iron metal-organic framework: 0.135 g FeCl.sub.3.6H.sub.2O was dissolved in 5 mL N,N-Dimethylformamide, and 0.041 g 1,4-benzenedicarboxylic acid was added, to obtain a mixture solution. The mixture solution was stirred until completely dissolved, then it was transferred into a 20 mL Teflon-lined high-pressure reactor, and then the high-pressure reactor was put into a thermostatic blast drying oven for reaction at 110 C. for 24 hours. After the high-pressure reactor was cooled to room temperature, the reaction solution was high-speed centrifuged at a speed of 10000 r to obtain a yellow solid. The solid was successively washed with absolute ethyl alcohol for 2 times, 3 hours per wash, and then it was put into a vacuum drying oven at 150 C. for drying for 12 hours, to obtain an iron metal-organic framework, labeled as MIL-101(Fe). 0.030 g0.152 g Cu(NO.sub.3).sub.2.3H.sub.2O and 0.036 g0.18 g Citric acid were successively weighed and were dissolved in 100 mL deionized water to obtain a solution, and then 0.4 g MIL-101(Fe) was added into the solution to obtain a mixture. The mixture was uniformly mixed by a magnetic stirrer for 4 hours, and then the mixture was transferred into a 100 mL Teflon-lined high-pressure reactor. The high-pressure reactor was put into the thermostatic blast drying oven for reaction at 80 C. for 8 hours. After the high-pressure reactor was cooled to room temperature, the reaction solution was high-speed centrifuged at a speed of 10000 r to obtain a solid. The solid was repeatedly washed with deionized water, until no blue color was found in washing liquid. The above obtained material was processed in a temperature programming tube furnace, with specific operation being: the tube furnace was rapidly heated to 200 C. in 25 min, and the material was high-temperature processed for 4 hours under the atmosphere of nitrogen; after the tube furnace was cooled to room temperature, the material was taken out, with the material being copper-doped iron metal-organic framework, labeled as Cu/MIL-101(Fe), and then it was stored in a dryer for later use.

(19) (1) As for 10% Cu/MIL-101(Fe), a conical flask was used as a reactor, and wastewater was 100 mL 0.1 mM/L AO7 solution. 0.02 g 10% copper-doped iron metal-organic framework and 0.238 g sodium persulfate (molar ratio PS/AO7=100) were added into the reactor simultaneously, and then the conical flask was put into a shaker with a speed of 180 rpm at a temperature of 25 C.

(20) (2) As for 8% Cu/MIL-101(Fe), the added catalyst was 0.02 g 8% copper-doped iron metal-organic framework, and the other conditions were consistent with the reaction system (1).

(21) (3) As for 6% Cu/MIL-101(Fe), the added catalyst was 0.02 g 6% copper-doped iron metal-organic framework, and the other conditions were consistent with the reaction system (1).

(22) (4) As for 4% Cu/MIL-101(Fe), the added catalyst was 0.02 g 4% copper-doped iron metal-organic framework, and the other conditions were consistent with the reaction system (1).

(23) The results of the four processes are shown in Table 2:

(24) TABLE-US-00002 TABLE 2 Removal Removal Removal Removal Time rate rate rate rate min %(10%) %(8%) %(6%) %(4%) 0 0 0 0 0 10 5.3 10.2 10.6 20.9 20 10.3 13.9 15.5 27.1 30 14.3 22.8 25.6 30.8 60 23.2 35.1 34.9 44.4 90 32.9 44.8 49.6 61.9 120 43.5 59.4 62.7 77.9 150 49.8 66.7 78.5 90.0 165 57.4 70.5 83.4 93.5 180 67.1 78.9 85.7 94.9 195 78.4 85 87.9 97.8 210 91.7 94.2 99.4 99.6

(25) The results in Table 2 illustrate that the four doping amounts have good removal efficiency on AO7. However, with the increasing copper doping amount, the removal rate of AO7 is slower. For example, at 180 min, removal rates corresponding to 4%, 6%, 8% and 10% copper doping amount is 94.9%, 85.7%, 78.9 and 67.1%, respectively. This may be due to the greater copper doping amount, the more copper ions into the pore of the iron metal-organic framework, thereby reducing the pore gap, affecting the reaction contact area, and thus delays the reaction rate. However, with the increase of reaction time, removal rates of AO7 of the four doping amounts all reach 90%. This table shows that the 4% copper doping amount has the best treatment effect.

(26) Embodiment 3

(27) The present embodiment used 10% copper-doped iron metal-organic framework as a catalyst, and compared the catalyst for removal rates of AO7 at different molar ratios of Na.sub.2S.sub.2O.sub.8 and AO7 (Na.sub.2S.sub.2O.sub.8/AO7=80, 100, 120, 140).

(28) The copper-doped iron metal-organic framework: 0.27 g FeCl.sub.3.6H.sub.2O was dissolved in 5 mL N,N-Dimethylformamide, and 0.082 g 1,4-benzenedicarboxylic acid was added, to obtain a mixture solution. The mixture solution was stirred until completely dissolved, then it was transferred into a 40 mL Teflon-lined high-pressure reactor, and then the high-pressure reactor was put into a thermostatic blast drying oven for reaction at 110 C. for 24 hours. After the high-pressure reactor was cooled to room temperature, a centrifuge with a speed of 9000 r was used for high-speed centrifuging to obtain a yellow solid. The solid was successively washed with absolute ethyl alcohol for 2 times, 3 hours per wash, and then it was put into a vacuum drying oven at 150 C. for drying for 12 hours, to obtain an iron metal-organic framework, labeled as MIL-101(Fe). 0.152 g Cu(NO.sub.3).sub.2.3H.sub.2O and 0.18 g Citric acid were successively weighed and were dissolved in 100 mL deionized water to obtain a solution, and then 0.4 g MIL-101(Fe) was added into the solution to obtain a mixture. The mixture was uniformly mixed by a magnetic stirrer for 4 hours, and then the mixture was transferred into a 100 mL Teflon-lined high-pressure reactor. The high-pressure reactor was put into a thermostatic blast drying oven for reaction at 80 C. for 8 hours. After the high-pressure reactor was cooled to room temperature, a centrifuge with a speed of 9000 r was used for high-speed centrifuging to obtain a solid. The solid was repeatedly washed with deionized water, until no blue color was found in washing liquid. The above obtained material was processed in a temperature programming tube furnace, with specific operation being: the tube furnace was rapidly heated to 200 C. in 25 min, and the material was high-temperature processed for 4 hours under the atmosphere of nitrogen; after the tube furnace was cooled to room temperature, the material was taken out, with the material being copper-doped iron metal-organic framework, labeled as 10% Cu/MIL-101(Fe), and then it was stored in a dryer for later use.

(29) (1) A conical flask was used as a reactor, and wastewater was 100 mL 0.1 mM/L AO7 solution. 0.02 g 10% copper-doped iron metal-organic framework and 0.1904 g sodium persulfate (molar ratio PS/AO7=80) were added into the reactor simultaneously, and then the conical flask was put into a shaker with a speed of 180 rpm at a temperature of 25 C.

(30) (2) 0.238 g (Na.sub.2S.sub.2O.sub.8/AO7=100) sodium persulfate was added, and the other conditions were the same as the reaction system (1).

(31) (3) 0.2856 g (Na.sub.2S.sub.2O.sub.8/AO7=120) sodium persulfate was added, and the other conditions were the same as the reaction system (1).

(32) (4) 0.3332 g (Na.sub.2S.sub.2O.sub.8/AO7=140) sodium persulfate was added, and the other conditions were the same as the reaction system (1).

(33) The results of the four processes are shown in Table 3.

(34) TABLE-US-00003 TABLE 3 Removal Removal Removal Removal Time rate rate rate rate min %(80) %(100) %(120) %(140) 0 0 0 0 0 10 3.2 5.8 6.4 8.5 20 6.8 7 7.8 11.7 30 12.7 11.1 12 14.6 60 17 18.6 17.7 19 90 23.1 25.4 25.6 28.3 120 29 38.4 33.8 30 135 38.3 49.5 46 38.5 150 50.8 58.2 59.8 51.2 165 58.1 69.3 71.9 68.8 180 64.6 78.3 82.4 78.3 210 84 93.5 90.1 91.2

(35) According to Table 3, it can be seen that when Na.sub.2S.sub.2O.sub.8/AO7=80, its removal rate is obviously lower than the other three cases, and when Na.sub.2S.sub.2O.sub.8/AO7=100, 120, 140, their removal rates are almost equivalent. For example, when the reaction time is 165 min, the removal rates of AO7 are about 70%; when the reaction time is 210 min, the removal rates AO7 reach more than 90%. Considering the catalytic effect of catalyst and the dosing cost of the drug, Na.sub.2S.sub.2O.sub.8/AO7=100 is the best choice.

(36) Embodiment 4

(37) The present embodiment used 6% copper-doped iron metal-organic framework as a catalyst, and compared the catalyst for removal rates of AO7 at different catalyst dosing quantities.

(38) The copper-doped iron metal-organic framework: 0.675 g FeCl.sub.3.6H.sub.2O was dissolved in 25 mL N,N-Dimethylformamide, and 0.206 g 1,4-benzenedicarboxylic acid was added, to obtain a mixture solution. The mixture solution was stirred until completely dissolved, then it was transferred into a 100 mL Teflon-lined high-pressure reactor, and then the high-pressure reactor was put into a thermostatic blast drying oven for reaction at 110 C. for 24 hours. After the high-pressure reactor was cooled to room temperature, a centrifuge with a speed of 8000 r was used for high-speed centrifuging to obtain a yellow solid. The solid was successively washed with absolute ethyl alcohol for 2 times, 3 hours per wash, and then it was put into a vacuum drying oven at 150 C. for drying for 12 hours, to obtain an iron metal-organic framework, labeled as MIL-101(Fe). 0.045 g Cu(NO.sub.3).sub.2.6H.sub.2O and 0.054 g Citric acid were successively weighed and were dissolved in 100 mL deionized water to obtain a solution, and then 0.2 g MIL-101(Fe) was added into the solution to obtain a mixture. The mixture was uniformly mixed by a magnetic stirrer for 4 hours, and then the mixture was transferred into a 100 mL Teflon-lined high-pressure reactor. The high-pressure reactor was put into a thermostatic blast drying oven for reaction at 80 C. for 8 hours. After the high-pressure reactor was cooled to room temperature, a centrifuge with a speed of 8000 r was used for high-speed centrifuging to obtain a solid. The solid was repeatedly washed with deionized water, until no blue color was found in washing liquid. The above obtained material was processed in a temperature programming tube furnace, with specific operation being: the tube furnace was rapidly heated to 240 C. in 30 min, and the material was high-temperature processed for 4 hours under the atmosphere of nitrogen; after the tube furnace was cooled to room temperature, the material was taken out, with the material being copper-doped iron metal-organic framework, labeled as 6% Cu/MIL-101(Fe), having an X-ray crystal diffraction pattern as shown in FIG. 2, and then it was stored in a dryer for later use.

(39) (1) A conical flask was used as a reactor, and wastewater was 100 mL 0.1 mM/L AO7 solution. 0.01 g 6% copper-doped iron metal-organic framework and 0.238 g sodium persulfate were added into the reactor simultaneously, and then the conical flask was put into a shaker with a speed of 180 rpm at a temperature of 25 C.

(40) (2) 0.02 g 6% copper-doped iron metal-organic framework was added, and the other conditions were consistent with the reaction system (1).

(41) (3) 0.04 g 6% copper-doped iron metal-organic framework was added, and the other conditions were consistent with the reaction system (1).

(42) (4) 0.06 g 6% copper-doped iron metal-organic framework was added, and the other conditions were consistent with the reaction system (1).

(43) The results of the four processes are shown in Table 4.

(44) TABLE-US-00004 TABLE 4 Removal Removal Removal Removal Time rate rate rate rate min % (0.01 g) % (0.02 g) % (0.04 g) % (0.06 g) 0 0 0 0 0 10 8.5 13.3 23.6 32.3 20 11.8 16.5 31.6 60.5 30 15.9 26.1 42 74.4 60 21.3 42.6 67.1 86.6 90 27.5 47.9 82.9 96.1 120 31.9 57.4 94.6 95.9 150 38 74.2 96.1 96.4 180 43.7 89.4 / / 210 51.2 97.8 / /

(45) It can be seen from Table 4 that, with the increasing catalyst dosing quantity, the rate of removal of AO7 is faster, the removal efficiency is also better. For example, at 150 min, removal rates corresponding to 0.01g, 0.02g, 0.04 g and 0.06 g catalyst are 38%, 74.2%, 96.1% and 96.4%, respectively.

(46) Embodiment 5

(47) The present embodiment used 8% copper-doped iron-based-metal-organic framework as a catalyst, and studied the influence of the number of recycle of the catalyst on removal rate of AO7.

(48) The copper-doped iron metal-organic framework: 0.675 g FeCl.sub.3.6H.sub.2O was dissolved in 25 mL N,N-Dimethylformamide, and 0.206 g 1,4-benzenedicarboxylic acid was added, to obtain a mixture solution. The mixture solution was stirred until completely dissolved, then it was transferred into a 100 mL Teflon-lined high-pressure reactor, and then the high-pressure reactor was put into a thermostatic blast drying oven for reaction at 110 C. for 24 hours. After the high-pressure reactor was cooled to room temperature, a centrifuge with a speed of 8000 r was used for high-speed centrifuging to obtain a yellow solid. The solid was successively washed with absolute ethyl alcohol for 2 times, 3 hours per wash, and then it was put into a vacuum drying oven at 150 C. for drying for 12 hours, to obtain an iron metal-organic framework, labeled as MIL-101(Fe). 0.09 g Cu(NO.sub.3).sub.2.6H.sub.2O and 0.108 g Citric acid were successively weighed and were dissolved in 100 mL deionized water to obtain a solution, and then 0.3 g MIL-101(Fe) was added into the solution to obtain a mixture. The mixture was uniformly mixed by a magnetic stirrer for 4 hours, and then the mixture was transferred into a 100 mL Teflon-lined high-pressure reactor. The high-pressure reactor was put into a thermostatic blast drying oven for reaction at 80 C. for 8 hours. After the high-pressure reactor was cooled to room temperature, a centrifuge with a speed of 10000 r was used for high-speed centrifuging to obtain a solid. The solid was repeatedly washed with deionized water, until no blue color was found in washing liquid. The above obtained material was processed in a temperature programming tube furnace, with specific operation being: the tube furnace was rapidly heated to 200 C. in 25 min, and the material was high-temperature processed for 4 hours under the atmosphere of nitrogen; after the tube furnace was cooled to room temperature, the material was taken out, with the material being copper-doped iron metal-organic framework, labeled as Cu/MIL-101(Fe), and then it was stored in a dryer for later use. An X-ray crystal diffraction pattern of the material is shown in FIG. 3.

(49) (1) A conical flask was used as a reactor, and wastewater was 100 mL 0.1 mM/L AO7 solution. 0.02 g 8% copper-doped iron metal-organic framework and 0.238 g potassium persulfate were added into the reactor simultaneously, and then the conical flask was put into a shaker with a speed of 180 rpm at a temperature of 25 C. Samples were taken at corresponding time points at 0, 30, 60, 90, 120, 150 and 180 min, respectively.

(50) (2) after step (1), the catalyst in the conical flask was high-speed centrifuged, dried in a drying oven at 60 C., and then put into 100 mL 0.1 mM/L AO7 solution. The other conditions were the same as the reaction system (1).

(51) (3) The catalyst was subjected to four recycles according to the method in the reaction system (1) and the reaction system (2), and its results of removal rate of AO7 was shown in Table 5.

(52) TABLE-US-00005 TABLE 5 Removal Removal Removal Removal rate rate rate rate Time % (first % (second % (third % (fourth min time) time) time) time) 0 0 0 0 0 30 0 28.1 19.5 15.7 60 34.1 43.9 33.5 22.6 90 46.6 58 58.2 42.9 120 75.8 72.7 77.1 65 150 85.8 83.7 85.1 78.1 180 96 91.4 90.2 86

(53) The results in Table 5 illustrate that the catalytic effect is still high even the catalyst has been subjected to four recycles. For example, at 180 min, the removal rates corresponding to the first, second, third and fourth times are 96%, 91.4%, 90.2% and 86.0%, respectively. The experiment shows that the copper-doped iron metal-organic framework has good reusability and provides the possibility of using the catalyst in the practical application of wastewater.