CN111871413A - Preparation and application of photocatalyst for degrading organic pollutants in water under alkaline condition - Google Patents

Preparation and application of photocatalyst for degrading organic pollutants in water under alkaline condition Download PDF

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CN111871413A
CN111871413A CN202010019905.9A CN202010019905A CN111871413A CN 111871413 A CN111871413 A CN 111871413A CN 202010019905 A CN202010019905 A CN 202010019905A CN 111871413 A CN111871413 A CN 111871413A
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soil
solution
photocatalyst
acid
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张竹青
朱宇
程桂茹
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Changchun University of Technology
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/745Iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/33Electric or magnetic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/03Precipitation; Co-precipitation
    • B01J37/031Precipitation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/722Oxidation by peroxides
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/02Specific form of oxidant
    • C02F2305/023Reactive oxygen species, singlet oxygen, OH radical
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/10Photocatalysts

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
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Abstract

A preparation method and an application of a photocatalyst for degrading organic matters in water under an alkaline condition relate to a preparation method and an application of a photocatalyst and aim to solve the problem that organic matters in wastewater are difficult to degrade under the existing alkaline condition. The method comprises the following steps: firstly, pickling diatomite raw soil, and removing impurities to obtain pickled soil; firing the acid-washed soil to obtain fired soil; modifying by using CTAB to obtain modified soil; and fourthly, loading the nano ferroferric oxide on the modified soil by using an in-situ coprecipitation method to obtain the loaded soil. The catalyst has low preparation cost and good organic pollutant removal effect. The invention is used for removing organic matters in the degraded alkaline wastewater.

Description

Preparation and application of photocatalyst for degrading organic pollutants in water under alkaline condition
Technical Field
The invention relates to a preparation method and application of a photocatalyst capable of degrading organic matters in water under an alkaline condition.
Background
The treatment of water pollution is always important in environmental protection. Water is an indispensable resource for human beings. The problem of water pollution has been a major concern. The water pollution problem is long-standing, the problem is acute, and the water pollution is complex, namely the pollution of inorganic substances and organic substances is included. The pollution of organic matters is difficult to treat, and the fundamental reason is that the organic matters are more in variety and different in properties and are difficult to solve by one method at one time.
The catalytic method is a development hotspot, and has the advantages that the primary conversion does not cause secondary pollution, secondary treatment is not needed, and the photocatalyst is a great class. However, since the photocatalyst is used under severe conditions, it is basically used under neutral and acidic conditions, and is rarely used under alkaline conditions. However, it is difficult to achieve all acidity or all neutrality depending on the place where the waste water is discharged. Therefore, the invention of the photocatalyst capable of efficiently degrading organic matters under the alkaline condition is particularly important.
Disclosure of Invention
The invention mainly solves the problem that the existing photocatalyst can not be applied under the alkaline condition, and provides a preparation method and application of a photocatalyst for degrading organic matters in water under the alkaline condition.
The invention discloses a preparation method of a photocatalyst for degrading organic matters in water under alkaline conditions, which is characterized by comprising the following steps:
firstly, acid washing of diatomite: preparing 30% sulfuric acid solution, placing diatomite in a beaker, adding 30% sulfuric acid solution, and immersing the diatomite. Heating to react for 1h at 90 ℃, and stirring intermittently. After the reaction is finished, cooling to room temperature, carrying out suction filtration, and washing while carrying out suction filtration until the diatomite is neutral. Drying at 100 deg.C, grinding, sealing and storing. Obtaining the acid-washed soil.
Firing acid-washing soil: and (4) taking a proper amount of acid-washed soil, and firing the acid-washed soil in a muffle furnace to obtain the burned soil.
Thirdly, CTAB modification: taking a proper amount of burnt soil, dissolving the burnt soil in deionized water, and ultrasonically dispersing for 0.5 h. According to the mass ratio of the burnt soil to the solid CTAB of 7: 3 ratio configuration 20
Figure 734234DEST_PATH_IMAGE001
t% CTAB solution. Added to the calcined soil solution and adjusted pH =11 using saturated sodium hydroxide solution. Stirring at 80 deg.C for 120 min. After the reaction is finished, cooling to room temperature and standing for 24 hours. Suction filtration and alternate washing with ethanol and deionized water until no foam is generated. Drying at 110 ℃ to obtain the modified soil.
Tetra, nano-tetraoxidePreparing iron-loaded soil: and preparing the nano ferroferric oxide loaded soil by using an in-situ coprecipitation method. Dissolving a certain amount of modified soil in deionized water, and performing ultrasonic dispersion for 5 min. Modifying soil according to the mass ratio: nano ferroferric oxide = 7: 3, calculating and weighing ferrous sulfate and ferric trichloride according to the proportion, respectively preparing the ferrous sulfate and the ferric trichloride into 0.1mol/L solution, and keeping Fe in the solution2+With Fe3+Always in a molar ratio of 3: 4. and introducing nitrogen for 5min to drive oxygen, and keeping introducing nitrogen all the time. The circulating cooling water was switched on, the stirring was switched on, and the temperature was maintained at 80 ℃. The reaction was stirred for 1h with pH =9-10 adjusted using saturated sodium hydroxide solution. The product was transferred to a beaker after cooling to room temperature and washed alternately with deionized water and absolute ethanol until the solution was neutral. And (5) drying in vacuum. Grinding and sieving with a 200-mesh sieve to obtain the nano ferroferric oxide loaded soil.
And step three, the ultrasonic power in step four is 40-60W.
Further, the burning temperature in the step two is 500-600 ℃.
Further, the burning time in the step two is 0-30min
The photocatalyst prepared by the method can be applied to degrading organic matters in wastewater under the alkaline condition.
The invention can degrade the organic matters in the alkaline wastewater, and the degradation efficiency can reach more than 99%.
The principle of the invention is as follows:
alkaline wastewater is used as one type of wastewater, because of the special pH value condition, the traditional photocatalyst can not be used for degradation treatment, if the alkaline wastewater is directly discharged without treatment, immeasurable loss can be caused to the ecological environment, and therefore, the photocatalyst capable of degrading organic matters in water under the alkaline condition is invented.
The main working principle of the catalyst in the process of degrading organic wastewater is that the diatomite has a large specific surface area, the specific surface area of a sample modified by CTAB is increased, the adsorption capacity is increased, the diatomite provides an active site through adsorption, the nano ferroferric oxide decomposes hydrogen peroxide under the action of sunlight irradiation to generate a hydrogen peroxide radical and a peroxy radical, and the two radicals have high redox potential and can effectively degrade organic matters in water, so that the degradation of the organic matters is realized.
The invention has the beneficial effects that:
the method takes diatomite as a raw material and adopts an in-situ coprecipitation synthesis method to prepare the photocatalyst. Therefore, the photocatalyst can be used for degrading organic matters in the alkaline wastewater.
The diatomite has good chemical stability and hydrophobicity and can be stably dispersed in water, so that the diatomite can show good stability and stably exist in the water, and is beneficial to adsorption and catalysis.
The invention is synthesized by an in-situ coprecipitation synthesis method, and has the advantages of simple preparation method, wide raw material source and simple operation. The product prepared by the in-situ coprecipitation synthesis method has magnetism and is beneficial to separation and reuse. The huge specific surface area of the diatomite is beneficial to adsorption and catalytic degradation of pollutants, so that the degradation efficiency of organic matters can reach more than 99%. The photocatalyst has good practicability and wide application prospect. .
The product prepared by the method has uniform size, simple synthesis method, cheap and easily-obtained raw materials and low cost, and the prepared product is non-toxic, has better photocatalytic performance and has wide application prospect in the fields of environment monitoring, treatment and the like and material chemistry.
Drawings
FIG. 1 is a scanning electron microscope image of the catalyst prepared in example 1 (the catalyst has a particle size of about 100. mu.m)
Figure 610923DEST_PATH_IMAGE002
m);
FIG. 2 is an XRD spectrum of the catalyst prepared in example 1;
FIG. 3 is an IR spectrum of the catalyst prepared in example 1
FIG. 4 is a kinetic curve of the catalytic reaction of the catalyst prepared in example 1 under basic conditions:
FIG. 5 is a plot of the number of uses of the catalyst prepared in example 1 under basic conditions;
Detailed Description
The technical solution of the present invention is not limited to the following specific embodiments, but includes any combination of the specific embodiments.
The first embodiment is as follows: the method for preparing the photocatalyst of the present embodiment is characterized by comprising the steps of:
firstly, acid washing of diatomite: preparing 30% sulfuric acid solution, placing diatomite in a beaker, adding 30% sulfuric acid solution, and immersing the diatomite. Heating to react for 1h at 90 ℃, and stirring intermittently. After the reaction is finished, cooling to room temperature, carrying out suction filtration, and washing with deionized water while carrying out suction filtration until the filtrate is neutral. The prepared sample is dried at 100 ℃, ground, sealed and stored. Obtaining the acid-washed soil.
Firing acid-washing soil: and (3) taking a proper amount of acid-washed soil, and burning the acid-washed soil in a muffle furnace at 500 ℃ to obtain burned soil.
Thirdly, CTAB modification: taking a proper amount of burnt soil, dissolving the burnt soil in deionized water, and ultrasonically dispersing for 0.5 h. According to the mass ratio of the burnt soil to the solid CTAB of 7: 3 ratio configuration 20
Figure 994238DEST_PATH_IMAGE001
t% CTAB solution. Added to the calcined soil solution and adjusted pH =11 using saturated sodium hydroxide solution. Stirring at 80 deg.C for 120 min. After the reaction is finished, cooling to room temperature and standing for 24 hours. Suction filtration and alternate washing with ethanol and deionized water until no foam is generated. Drying at 110 ℃ to obtain the modified soil.
Preparing the nano ferroferric oxide loaded soil: and preparing the nano ferroferric oxide loaded soil by using an in-situ coprecipitation method. Dissolving a certain amount of modified soil in deionized water, and performing ultrasonic dispersion for 5 min. The modified soil comprises the following components in percentage by mass: nano ferroferric oxide = 7: 3, calculating and weighing ferrous sulfate and ferric trichloride according to the proportion, respectively preparing the ferrous sulfate and the ferric trichloride into 0.1mol/L solution, and keeping Fe in the solution2+With Fe3+Always in a molar ratio of 3: 4. introducing nitrogen for 5min to drive oxygen, andthe nitrogen was kept constantly introduced. The circulating cooling water was turned on, stirring was started, and the temperature was maintained at 80 ℃. The reaction was stirred for 1h with pH =9-10 adjusted using saturated sodium hydroxide solution. The product was transferred to a beaker after cooling to room temperature and washed alternately with deionized water and absolute ethanol until the solution was neutral. Vacuum drying, grinding and sieving with a 200-mesh sieve to obtain the nano ferroferric oxide loaded soil.
The following examples are given to illustrate the present invention, and the following examples are carried out on the premise of the technical solution of the present invention, and give detailed embodiments and specific procedures, but the scope of the present invention is not limited to the following examples.
Example 1:
firstly, acid washing of diatomite: preparing 30% sulfuric acid solution, placing diatomite in a beaker, adding 30% sulfuric acid solution, and immersing the diatomite. Heating to react for 1h at 90 ℃ and stirring intermittently. After the reaction is finished, cooling to room temperature, carrying out suction filtration, and washing while carrying out suction filtration until the filtrate is neutral. Drying at 100 deg.C, grinding, sealing and storing. Obtaining the acid-washed soil.
Firing acid-washing soil: and (3) taking a proper amount of acid-washed soil, and burning the acid-washed soil in a muffle furnace at 500 ℃ to obtain burned soil.
Thirdly, CTAB modification: taking a proper amount of burnt soil, dissolving the burnt soil in deionized water, and ultrasonically dispersing for 0.5 h. According to the mass ratio of the burnt soil to the solid CTAB of 7: 3 ratio configuration 20
Figure 261271DEST_PATH_IMAGE001
t% CTAB solution. Added to the calcined soil solution and adjusted pH =11 using saturated sodium hydroxide solution. Stirring at 80 deg.C for 120 min. After the reaction is finished, cooling to room temperature and standing for 24 hours. Suction filtration and alternate washing with ethanol and deionized water until no foam is generated. Drying at 110 ℃. Obtaining the modified soil.
Preparing the nano ferroferric oxide loaded soil: and preparing the nano ferroferric oxide loaded soil by using an in-situ coprecipitation method. Dissolving a certain amount of modified soil in deionized water, and performing ultrasonic dispersion for 5 min. Modifying soil according to the mass ratio: nano ferroferric oxide = 7: 3 and weighing sulfuric acidIron and ferric trichloride are respectively prepared into 0.1mol/L solution, and Fe in the solution is maintained2+With Fe3+Always in a molar ratio of 3: 4. and introducing nitrogen for 5min to drive oxygen, and keeping introducing nitrogen all the time. The circulating cooling water was turned on, stirring was started, and the temperature was maintained at 80 ℃. The reaction was stirred for 1h with the pH =9-10 adjusted using bag and sodium hydroxide solution. The product was transferred to a beaker after cooling to room temperature and washed alternately with deionized water and absolute ethanol until the solution was neutral. Vacuum drying, grinding and sieving with a 200-mesh sieve to obtain the nano ferroferric oxide loaded soil.
The scanning electron micrograph of the catalyst prepared in this example is shown in FIG. 1, and the catalyst has uniform size and good dispersibility, and the size is about 100
Figure 460171DEST_PATH_IMAGE002
m。
Fig. 2 is an XRD spectrum of the catalyst prepared in this example, and it can be seen that the loading was successful.
FIG. 3 is an IR spectrum of the catalyst prepared in this example, and the success of the preparation can be seen
FIG. 4 is a graph showing the reaction rate of the catalyst prepared in this example, and it can be seen that the reaction is a first-order reaction and the reaction rate is relatively high.
Fig. 5 is a reaction use frequency curve of the catalyst prepared in this example, and the degradation efficiency can still reach more than 95% after repeated use, which shows that the catalyst has good catalytic efficiency.

Claims (6)

1. Firstly, acid washing of diatomite: preparing a 30% sulfuric acid solution, putting diatomite into a beaker, adding the 30% sulfuric acid solution, immersing the diatomite, heating to react for 1h at 90 ℃, and intermittently stirring; after the reaction is finished, cooling to room temperature, carrying out suction filtration, washing with deionized water while carrying out suction filtration until the filtrate is neutral, drying at 100 ℃, grinding, and carrying out sealed preservation to obtain acid-washed soil; firing acid-washing soil: taking a proper amount of acid-washed soil, and firing the acid-washed soil in a muffle furnace to obtain burned soil; thirdly, CTAB modification: taking a proper amount of burning soil, dissolving the burning soil with deionized water, and ultrasonically dispersing for 0.5h, wherein the mass ratio of the burning soil to solid CTAB is 7: 3 ratio configuration 20
Figure DEST_PATH_IMAGE001
Adding a t% CTAB solution into the burned soil solution, adjusting the pH to be =11 by using a saturated sodium hydroxide solution, and stirring at the constant temperature of 80 ℃ for 120 min; cooling to room temperature after the reaction is finished, standing for 24h, performing suction filtration, alternately washing with ethanol and deionized water until no foam is generated, and drying at 110 ℃ to obtain modified soil; preparing the nano ferroferric oxide loaded soil: preparing nano ferroferric oxide loaded soil by using an in-situ coprecipitation method; dissolving a certain amount of modified soil in deionized water, and performing ultrasonic dispersion for 5 min; modifying soil according to the mass ratio: nano ferroferric oxide = 7: 3, calculating and weighing ferrous sulfate and ferric trichloride according to the proportion, respectively preparing the ferrous sulfate and the ferric trichloride into 0.1mol/L solution, and keeping Fe in the solution2+With Fe3+Always in a molar ratio of 3: 4; introducing nitrogen for 5min to drive oxygen, and keeping introducing nitrogen all the time; connecting circulating cooling water, starting stirring, and maintaining the temperature at 80 ℃; adjusting the pH to be 9-10 by using saturated sodium hydroxide solution, and stirring for reaction for 1 h; cooling to room temperature, transferring the product into a beaker, and alternately washing the product with deionized water and absolute ethyl alcohol in sequence until the solution is neutral; vacuum drying; grinding and sieving with a 200-mesh sieve to obtain the nano ferroferric oxide loaded soil.
2. The method for preparing the photocatalyst for degrading alkaline wastewater according to claim 1, wherein the ultrasonic power in the third step and the ultrasonic power in the fourth step are 40-60W.
3. The method as claimed in claim 2, wherein the burning temperature in step two is 500-600 ℃.
4. The method according to claim 3, wherein the burning time in step two is 0-30 min.
5. The method for preparing the photocatalyst for degrading alkaline wastewater according to claim 4, wherein CTAB is used for modification in the third step.
6. The photocatalyst prepared by the method of claim 1 is used for degradation treatment of wastewater under alkaline conditions.
CN202010019905.9A 2020-01-09 2020-01-09 Preparation and application of photocatalyst for degrading organic pollutants in water under alkaline condition Pending CN111871413A (en)

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