CN115417487A - Li 2 MnO 3 Application of BPA in catalytic activation of peroxymonosulfate to degradation of BPA - Google Patents
Li 2 MnO 3 Application of BPA in catalytic activation of peroxymonosulfate to degradation of BPA Download PDFInfo
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- CN115417487A CN115417487A CN202211029326.8A CN202211029326A CN115417487A CN 115417487 A CN115417487 A CN 115417487A CN 202211029326 A CN202211029326 A CN 202211029326A CN 115417487 A CN115417487 A CN 115417487A
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- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/722—Oxidation by peroxides
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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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
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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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
- B01J37/082—Decomposition and pyrolysis
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- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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- 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
- C02F2101/34—Organic compounds containing oxygen
- C02F2101/345—Phenols
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Abstract
The invention discloses a catalyst Li 2 MnO 3 Application of activating peroxymonosulfate to degrade BPA, and catalyst Li 2 MnO 3 The preparation method comprises the step of preparing Li by adopting a solid-phase sintering method 2 MnO 3 Sintering the mixture in a muffle furnace at the constant temperature of 900 ℃ for 10 hours, and naturally cooling the mixture to room temperature to obtain the product. The catalyst Li 2 MnO 3 The catalyst has good catalytic effect on the aspect of activating peroxymonosulfate to degrade BPA, and has stable catalytic property.
Description
Technical Field
The invention belongs to the technical field of environmental protection and pollutant degradation, and particularly relates to a catalyst Li 2 MnO 3 Application for catalyzing and activating peroxymonosulfate to degrade BPA and a preparation method thereof.
Background
In recent years, water pollutionThe pollution problem is increasingly serious, and especially the concentration of residual antibiotics in the water body is excessive and exceeds the standard, which causes serious harm to the life of people. To overcome these challenges, in the past decades, peroxymonosulfate (PMS) based, because of its good stability, low cost and ease of transportation, has become a promising oxidant whose activation to generate Reactive Oxygen Species (ROS) is of increasing interest for degrading or mineralizing recalcitrant organic pollutants in various industrial and consumer applications. A number of supported and unsupported metals or metal oxides have been developed as PMS activators, including MnO 2 、CuO-Fe 3 O 4 、Pd/Al 2 O 3 And the like. Magnetic metal nanoparticles are easily aggregated, thereby reducing their catalytic activity. The release of metal ions based on cobalt oxide and the like can also lead to secondary water contamination. The synthesis of supported metal catalysts typically involves complex processes and multiple reagents, often requiring long preparation times. Therefore, it remains necessary to expand the scope of heterogeneous catalysts for activating PMS by developing other metal/metal oxide materials. The search and preparation of highly efficient and stable catalysts for activating PMS is the hot spot of current research.
Bisphenol A (BPA) is one of the most widely used industrial compounds in the world, and is mainly used for producing various high polymer materials such as polycarbonate, epoxy resin, polysulfone resin, polyphenylene oxide resin, unsaturated polyester resin and the like. Can also be used for producing fine chemical products such as plasticizer, flame retardant, antioxidant, heat stabilizer, rubber antioxidant, pesticide, coating and the like.
In the manufacturing process of plastic products, the addition of bisphenol A can make the plastic products have the characteristics of colorless transparency, durability, lightness, outstanding impact resistance and the like, and particularly can prevent acidic vegetables and fruits from corroding metal containers from the inside, so the bisphenol A is widely used in the manufacturing process of packages of canned foods and beverages, sealing glue for feeding bottles, water bottles and tooth fillers, spectacle lenses and other hundreds of daily necessities. Thus, BPA is ubiquitous, ranging from mineral water bottles, medical devices, and the interior of food packaging, all of which have their silhouettes. It can be seen that BPA residues are relatively common and cause environmental pollution, and particularly BPA residues are easy to remain in water and need to be treated in an environment-friendly way.
Li 2 MnO 3 The method is mainly used for electrochemical application, in particular to the preparation of a positive electrode material for a lithium battery. However, the present inventors have unexpectedly found that Li synthesized by a solid phase sintering method 2 MnO 3 Research shows that Li 2 MnO 3 The PMS system has higher and stable catalytic activity, and is very effective in activating peroxymonosulfate to degrade residual BPA, especially residual BPA in water.
Disclosure of Invention
The invention aims to provide Li 2 MnO 3 Use of peroxomonosulfate as catalyst for degrading BPA (bisphenol A), preparation method thereof, and Li 2 MnO 3 A preparation method. The catalyst is mainly applied to the field of environmental protection restoration, and is particularly used for degrading residual BPA in water.
In one embodiment, the present invention provides a catalyst, li 2 MnO 3 Use for catalytically activating peroxymonosulfate to degrade BPA.
In the above-mentioned use of the present invention, the peroxymonosulfate is oxone (also known as "potassium monopersulfate" or "potassium peroxymonosulfate").
The use of the invention, the catalyst Li 2 MnO 3 Has the characteristic peak shown in figure 1.
In another embodiment, the present invention also provides a catalyst, li 2 MnO 3 The preparation method comprises the following steps:
(1) Mixing Li 2 CO 3 And MnCO 3 According to the mol ratio of 1:1, grinding after mixing;
(2) After being uniformly ground, the mixture is placed in a muffle furnace to be heated to 900 ℃ for constant-temperature sintering reaction;
(3) After the reaction is finished, naturally cooling to room temperature to obtain red powdery Li 2 MnO 3 。
In the method of the present invention, in the step (1), the grinding time is 40min, and in the step (2), the temperature is raised at a rate of 5 ℃/min. The sintering time is 10h.
In particular embodiments, a catalyst of the present invention, li 2 MnO 3 The preparation method comprises the following steps:
(1) Mixing Li 2 CO 3 And MnCO 3 According to a certain molar ratio of 3:3, after weighing, placing the mixture in an agate mortar for uniform mixing and grinding;
(2) Placing the uniformly ground mixture in a crucible, and then placing the crucible in a muffle furnace to heat to 900 ℃ for constant-temperature sintering reaction for 10 hours;
(3) After the reaction is finished, naturally cooling to room temperature to obtain red powdery Li 2 MnO 3 。
In the above embodiment, the method of the present invention, the grinding time in the step (1) is 40min, and the temperature in the step (2) is increased at a rate of 5 ℃/min.
On the other hand, catalyst Li 2 MnO 3 Use of the catalyst Li in the catalytic degradation of BPA by activated PMS (peroxymonosulfate) 2 MnO 3 Is prepared by the method of the invention.
Preferably, the use according to the invention is a catalyst Li 2 MnO 3 The application of the catalyst in activating PMS (potassium hydrogen persulfate) to catalytically degrade alkylphenol BPA.
The invention utilizes the catalyst Li prepared by a solid-phase sintering method 2 MnO 3 The application of the activated PMS in catalytic degradation of BPA, particularly in degradation of residual pollutants in environmental water, preferably BPA.
In another embodiment, a catalyst of the present invention, li 2 MnO 3 The preparation method comprises the following steps:
(1) 3mmol of Li were weighed out separately 2 CO 3 、3mmol MnCO 3 Mixing and grinding for 40min, and transferring to a corundum crucible;
(2) Putting the corundum crucible into a high-temperature muffle furnace, heating to 900 ℃ at the heating rate of 5 ℃/min, sintering for 10 hours, naturally cooling to room temperature, and finally obtaining Li 2 MnO 3 ;
The invention has the beneficial effects that:catalyst Li obtained by solid-phase sintering 2 MnO 3 The catalyst has good catalytic degradation effect on antibiotics, particularly BPA, is particularly used for degrading BPA medicines in water pollutants, is beneficial to environmental protection treatment, can be recycled, and has stable catalytic property.
Drawings
FIG. 1 Li prepared in example 1 2 MnO 3 XRD pattern of (a);
FIG. 2 catalyst Li 2 MnO 3 ,MnCO 3 A catalytic degradation diagram of activating PMS to degrade BPA;
FIG. 3Li 2 MnO 3 XRD contrast patterns before and after PMS activation degradation BPA reaction, wherein the upper pattern is Li before catalytic reaction 2 MnO 3 The lower spectrum is Li after catalytic reaction 2 MnO 3 XRD pattern of (a).
Detailed Description
The following examples are exemplary and are included to aid in understanding and further illustrate the spirit of the invention, but are not intended to limit the scope of the invention.
It should be noted that the experimental methods used in the following examples are all conventional methods unless otherwise specified; materials, reagents, equipment and the like used in the following examples are commercially available unless otherwise specified.
Li used in the examples 2 CO 3 99.90% pure from alatin; mnCO 3 99.90% pure from alatin; the purity of the potassium hydrogen persulfate is 42 to 46 percent 5 basis, from alatin; bisphenol A with a purity of 99.0% from alatin; the methanol has purity of AR 99.5% and is from chemical industry of Chuandong.
Example 1 solid phase method for preparing Li 2 MnO 3
The preparation process comprises the following steps:
(1) 3mmol of Li were weighed out separately 2 CO 3 、3mmol MnCO 3 Mixing and grinding for 40min, and transferring to a corundum crucible;
(2) Putting the corundum crucible into a high-temperature muffle furnace, and keeping the temperature rise at 5 ℃Heating to 900 ℃ in min, sintering and reacting for 10h, naturally cooling to room temperature after the reaction is finished, and finally obtaining the product catalyst Li 2 MnO 3 。
XRD test: taking the obtained product Li 2 MnO 3 After a small amount of the product was sufficiently ground in an agate mortar, the sample was subjected to phase characterization on a Shimadzu 7000-X-ray diffractometer, and the XRD (X-ray powder diffraction pattern) result thereof is shown in FIG. 1.
Example 2 application Effect test
1. By implementing the experiment of activating PMS to catalytically degrade BPA, li prepared by solid-phase sintering can be known 2 MnO 3 the/PMS (potassium hydrogen persulfate) system has good degradation effect on BPA. Originally using Li 2 MnO 3 PMS and MnCO 3 PMS, li only 2 MnO 3 The results of the comparative experiment with PMS alone are shown in FIG. 2, and Li can be seen within 90min 2 MnO 3 The degradation rate of (70 mg)/PMS (potassium hydrogen persulfate) (6 mg) system to BPA (20 mg/L) can reach 80%. The cycle experiment shows that Li 2 MnO 3 Has stable catalytic oxidation degradation efficiency. Compared with MnCO 3 The catalytic oxidation degradation efficiency is greatly improved.
2. The experiment comprises the following specific steps:
taking 70mg of the prepared catalyst Li 2 MnO 3 Adding into 100ml BPA solution with concentration of 20mg/L, dark adsorbing for 60min to establish adsorption-desorption equilibrium. Adding 6mg PMS (potassium hydrogen persulfate) after dark adsorption for reacting for 90min, taking 2mL of supernatant every 15min for the first 60min and 30min for the last one, placing the supernatant in a centrifuge tube prepared with 2mL of methanol, centrifuging, filtering with a 0.22um filter membrane, and measuring the peak area by a high performance liquid chromatograph (Agilent 1260). The result shows that the degradation efficiency reaches 80% within 90min, and the degradation effect is good.
Taking 70mg of MnCO 3 (i.e. preparation of catalyst Li) 2 MnO 3 Raw material (b) was added to 100ml of BPA solution having a concentration of 20mg/L, and adsorption-desorption equilibrium was established for 60min by dark adsorption. Adding 6mg PMS (potassium hydrogen persulfate) after dark adsorption for reaction for 90min, taking 2mL supernatant every 15min for the first 60min, and taking the supernatant at 30min intervals for the last one, and placing the supernatant in the place where the supernatant has been removedCentrifuging in a centrifuge tube containing 2mL of methanol, filtering with 0.22um filter membrane, and measuring its peak area with high performance liquid chromatograph (Agilent 1260). The result shows that the catalytic degradation-oxidation decomposition efficiency is only 20 percent in 90min relative to Li 2 MnO 3 The catalytic oxidation degradation efficiency is reduced by 60 percent. Illustrating the Li prepared 2 MnO 3 The catalyst can greatly improve the degradation effect of BPA.
The circulation experiment proves Li 2 MnO 3 Reproducibility and stability of catalytic activity of PMS for degradation of BPA.
Further, catalyst Li was investigated 2 MnO 3 Phase stability after cyclic reaction of activated PMS (potassium hydrogen persulfate) degradation experiment. FIG. 3 shows the catalyst Li 2 MnO 3 XRD patterns before and after catalytic reaction show that the catalyst Li 2 MnO 3 The crystal form structure remains unchanged after the cyclic catalysis test, and the crystal form structure has good phase stability and cyclic usability. Thus, the catalyst Li prepared by the solid-phase sintering method 2 MnO 3 Can be recycled to treat and remove the residual antibiotic BPA pollutants in the water body, thereby continuously protecting the environment.
Claims (7)
1. Catalyst Li 2 MnO 3 Use for catalytically activating peroxymonosulfate to degrade BPA.
2. The use according to claim 1, wherein the peroxymonosulfate is oxone.
3. The use according to claim 1, said Li 2 MnO 3 Has the characteristic peaks shown in figure 1.
4. Preparation of the catalyst Li according to claim 1 2 MnO 3 The method comprises the following steps:
(1) Mixing Li 2 CO 3 And MnCO 3 According to the mol ratio of 1:1, grinding after mixing;
(2) After being uniformly ground, the mixture is placed in a muffle furnace to be heated to 900 ℃ for constant-temperature sintering reaction;
(3) After the reaction is finished, naturally cooling to room temperature to obtain red powdery Li 2 MnO 3 。
5. The method of claim 4, wherein in step (1), the milling time is 40min.
6. The method of claim 4, wherein in step (2), the sintering time is 10 hours.
7. The method according to claim 4, wherein in the step (2), the temperature is increased at a rate of 5 ℃/min.
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