CN109399726B - Preparation method of iron lanthanum oxide molecular sieve type purification material - Google Patents

Preparation method of iron lanthanum oxide molecular sieve type purification material Download PDF

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CN109399726B
CN109399726B CN201811358610.3A CN201811358610A CN109399726B CN 109399726 B CN109399726 B CN 109399726B CN 201811358610 A CN201811358610 A CN 201811358610A CN 109399726 B CN109399726 B CN 109399726B
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iron lanthanum
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CN109399726A (en
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张文杰
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Shenyang Ligong University
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/0018Mixed oxides or hydroxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8668Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • 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
    • 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
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/80Type of catalytic reaction
    • B01D2255/802Photocatalytic

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Abstract

A preparation method of an iron lanthanum oxide molecular sieve type purification material belongs to the field of environment-friendly purification materials, and comprises the following steps: preparing a solution A from absolute ethyl alcohol, polyethylene glycol, hexadecyl trimethyl ammonium bromide and Span60, preparing a solution B from deionized water, lanthanum acetate, ferric trichloride, polyacrylamide and sodium dihydrogen phosphate, and mixing the solution A and the solution B to obtain an iron lanthanum precursor; carrying out hydrothermal reaction, filtering, drying and calcining on the iron lanthanum precursor to obtain a solid; and (3) treating the solid with a phosphoric acid solution, and drying to obtain the iron lanthanum oxide molecular sieve type purification material. The purifying material has large specific surface area and porous characteristic, can fully adsorb organic pollutants in water and air, and can rapidly and effectively decompose organic matters under illumination.

Description

Preparation method of iron lanthanum oxide molecular sieve type purification material
Technical Field
The invention belongs to the field of environment-friendly purification materials, and particularly relates to a preparation method of an iron lanthanum oxide molecular sieve type purification material.
Background
Due to the wide use of various toxic and harmful artificially synthesized organic pollutants, more and more organic pollutants enter water, atmosphere and other global environments, and the pollutants in drinking water and indoor air cause great harm to human health, which has caused great concern to people. The environment-friendly purifying material is a functional material which can be used for purifying pollution, and the action mechanism of the environment-friendly purifying material comprises adsorption, filtration, flocculation, oxidation and the like. The most widely used environmental-friendly purification materials are various adsorbents which can adsorb and remove organic pollutants. However, such materials do not have a continuous purification capacity, and must be regenerated after saturation of adsorption, and the adsorbed organic substances are removed by a regeneration procedure to restore the adsorption capacity of the material. In order to make the environmental-friendly purification material have a longer service life, the environmental-friendly purification material needs to have the activity of decomposing organic pollutants, namely, the environmental-friendly purification material can adsorb and decompose organic matters at the same time, and the material has huge application prospects.
Disclosure of Invention
Aiming at the problems in the prior art, the invention aims to provide a preparation method of an iron lanthanum oxide molecular sieve type purification material, which can be used for purifying organic pollutants in water and air. The purifying material can adsorb organic matter and degrade the organic matter under illumination, and is suitable for various water and air pollution purifying fields.
A preparation method of an iron lanthanum oxide molecular sieve type purification material comprises the following preparation steps.
Step 1: preparing iron lanthanum precursor.
(1) Adding 7-10 g of polyethylene glycol 20000, 1.5-2 g of hexadecyl trimethyl ammonium bromide and 3-5 g of emulsifier Span60 into 200mL of absolute ethyl alcohol, and stirring to form a solution A.
(2) Adding 8-11 g of lanthanum acetate, 12-15 g of ferric trichloride, 3-6 g of polyacrylamide with the molecular weight of 200 ten thousand and 3.5-4.5 g of sodium dihydrogen phosphate into 280mL of deionized water, and stirring to form a solution B.
(3) And mixing the solution A and the solution B to obtain the iron lanthanum precursor.
Step 2: and (5) carrying out hydrothermal forming.
And (3) moving the iron lanthanum precursor into a stainless steel hydrothermal reaction kettle, reacting for 60 hours at 260-270 ℃, cooling, filtering, and drying the obtained solid substance for 20 hours at 190 ℃ to obtain a solid substance A.
And step 3: and (4) calcining and crystallizing.
And calcining the solid A at 800-850 ℃ for 6h, and cooling to obtain a solid B.
And 4, step 4: and (4) activating.
Mixing the solid B with 700mL of 0.6mol/L phosphoric acid solution, heating to 85 ℃, preserving the temperature for 200min, filtering, and drying the obtained solid substance at 190 ℃ for 20h to obtain the iron lanthanum oxide molecular sieve type purification material.
The prepared iron lanthanum oxide molecular sieve type purification material has the following technical characteristics: pore size is 6-7 nm, and specific surface area is 520-760 m2Per g, pore volume of 0.5-0.6 cm3(ii) a bulk density of 0.9 to 1.0g/cm3
Compared with the prior art, the preparation method of the iron lanthanum oxide molecular sieve type purification material has the advantages that: iron lanthanum oxide has photocatalytic purification activity, but the related materials prepared in general are not highly active due to lack of regular pore structure. The invention adopts a reasonable preparation process, takes iron lanthanum oxide as a basic framework composition, and forms a regular porous characteristic with a molecular sieve structure in the material. Fe-O-La forms a ring structure and forms a specific hollow cage structure by extending in a three-dimensional space. The opening size of the Fe-O-La ring is 6-7 nm. After the molecular sieve type structure is formed, the iron lanthanum oxide can fully adsorb organic pollutants in water and air, and can quickly and effectively decompose organic matters under illumination, so that the effect of continuously and quickly purifying the organic pollutants is achieved.
Detailed Description
Example 1.
A preparation method of an iron lanthanum oxide molecular sieve type purification material mainly comprises the following steps.
Step 1: preparing iron lanthanum precursor.
(1) To 200mL of absolute ethanol were added 7g of polyethylene glycol 20000, 1.5g of cetyltrimethylammonium bromide and 3g of emulsifier Span60, followed by stirring to obtain a solution A.
(2) 8g of lanthanum acetate, 12g of ferric trichloride, 3g of polyacrylamide with the molecular weight of 200 ten thousand and 3.5g of sodium dihydrogen phosphate are added into 280mL of deionized water, and stirred to form a solution B.
(3) And mixing the solution A and the solution B to obtain the iron lanthanum precursor.
Step 2: and (5) carrying out hydrothermal forming.
And (3) moving the iron lanthanum precursor into a stainless steel hydrothermal reaction kettle, reacting for 60h at 260 ℃, cooling, filtering, and drying the obtained solid substance for 20h at 190 ℃ to obtain a solid substance A.
And step 3: and (4) calcining and crystallizing.
Calcining the solid A at 800 ℃ for 6h, and cooling to obtain a solid B.
And 4, step 4: and (4) activating.
Mixing the solid B with 700mL of 0.6mol/L phosphoric acid solution, heating to 85 ℃, preserving the temperature for 200min, filtering, and drying the obtained solid substance at 190 ℃ for 20h to obtain the iron lanthanum oxide molecular sieve type purification material.
The prepared iron lanthanum oxide molecular sieve type purification material has the following technical characteristics: pore size 6nm and specific surface area 520m2G, pore volume 0.5cm3(g), bulk density 0.9g/cm3
And (5) detecting the performance.
20mg of the purification material prepared in example 1 was added to 100mL of a methyl orange solution having a concentration of 10mg/L, and the mixture was stirred in the dark for 60min to determine the concentration of the methyl orange solution; the solution was then placed under a 150W tungsten halogen lamp and the methyl orange solution concentration was measured every 10 min. And calculating the adsorption rate and the photocatalytic degradation rate of the methyl orange on the purification material.
According to the measurement result, the equilibrium saturation adsorption rate of the methyl orange on the purification material is 6.5%. After irradiation under a halogen tungsten lamp, methyl orange generates photocatalytic degradation reaction on the purification material; after 30min of photocatalytic degradation reaction, the photocatalytic degradation rate of the methyl orange solution reaches 100%.
Example 2.
A preparation method of an iron lanthanum oxide molecular sieve type purification material mainly comprises the following steps.
Step 1: preparing iron lanthanum precursor.
(1) To 200mL of absolute ethanol were added 8.5g of polyethylene glycol 20000, 1.7g of cetyltrimethylammonium bromide and 4g of emulsifier Span60, followed by stirring to obtain a solution A.
(2) 9g of lanthanum acetate, 13g of ferric chloride, 4.5g of polyacrylamide with the molecular weight of 200 ten thousand and 4g of sodium dihydrogen phosphate are added into 280mL of deionized water, and stirred to form a solution B.
(3) And mixing the solution A and the solution B to obtain the iron lanthanum precursor.
Step 2: and (5) carrying out hydrothermal forming.
And (3) moving the iron lanthanum precursor into a stainless steel hydrothermal reaction kettle, reacting for 60h at 265 ℃, cooling, filtering, and drying the obtained solid substance for 20h at 190 ℃ to obtain a solid substance A.
And step 3: and (4) calcining and crystallizing.
The solid A was calcined at 820 ℃ for 6h and cooled to give solid B.
And 4, step 4: and (4) activating.
Mixing the solid B with 700mL of 0.6mol/L phosphoric acid solution, heating to 85 ℃, preserving the temperature for 200min, filtering, and drying the obtained solid substance at 190 ℃ for 20h to obtain the iron lanthanum oxide molecular sieve type purification material.
The prepared iron lanthanum oxide molecular sieve type purification material has the following technical characteristics: pore size 6nm, specific surface area 630m2G, pore volume 0.5cm3(g), bulk density 0.9g/cm3
Example 3.
A preparation method of an iron lanthanum oxide molecular sieve type purification material mainly comprises the following steps.
Step 1: preparing iron lanthanum precursor.
(1) 10g of polyethylene glycol 20000, 2g of cetyltrimethylammonium bromide and 5g of emulsifier Span60 were added to 200mL of anhydrous ethanol, and stirred to form a solution A.
(2) 11g of lanthanum acetate, 15g of ferric trichloride, 6g of polyacrylamide with the molecular weight of 200 ten thousand and 4.5g of sodium dihydrogen phosphate are added into 280mL of deionized water, and stirred to form a solution B.
(3) And mixing the solution A and the solution B to obtain the iron lanthanum precursor.
Step 2: and (5) carrying out hydrothermal forming.
And (3) moving the iron lanthanum precursor into a stainless steel hydrothermal reaction kettle, reacting for 60h at 270 ℃, cooling, filtering, and drying the obtained solid substance for 20h at 190 ℃ to obtain a solid substance A.
And step 3: and (4) calcining and crystallizing.
Calcining the solid A at 850 ℃ for 6h, and cooling to obtain a solid B.
And 4, step 4: and (4) activating.
Mixing the solid B with 700mL of 0.6mol/L phosphoric acid solution, heating to 85 ℃, preserving the temperature for 200min, filtering, and drying the obtained solid substance at 190 ℃ for 20h to obtain the iron lanthanum oxide molecular sieve type purification material.
The prepared iron lanthanum oxide molecular sieve type purification material has the following technical characteristics: pore size 7nm, specific surface area 760m2G, pore volume 0.6cm3(g), bulk density 1.0g/cm3

Claims (2)

1. The preparation method of the iron lanthanum oxide molecular sieve type purification material is characterized by comprising the following process steps:
step 1: preparation of iron lanthanum precursor
(1) Adding 7-10 g of polyethylene glycol 20000, 1.5-2 g of hexadecyl trimethyl ammonium bromide and 3-5 g of emulsifier Span60 into 200mL of absolute ethyl alcohol, and stirring to form a solution A;
(2) adding 8-11 g of lanthanum acetate, 12-15 g of ferric trichloride, 3-6 g of polyacrylamide with the molecular weight of 200 ten thousand and 3.5-4.5 g of sodium dihydrogen phosphate into 280mL of deionized water, and stirring to form a solution B;
(3) mixing the solution A and the solution B to obtain an iron lanthanum precursor;
step 2: hydrothermal forming
Moving the iron lanthanum precursor into a stainless steel hydrothermal reaction kettle, reacting for 60 hours at 260-270 ℃, cooling, filtering, and drying the obtained solid substance for 20 hours at 190 ℃ to obtain a solid substance A;
and step 3: calcined crystals
Calcining the solid A at 800-850 ℃ for 6h, and cooling to obtain a solid B;
and 4, step 4: activation of
Mixing the solid B with 700mL of 0.6mol/L phosphoric acid solution, heating to 85 ℃, preserving the temperature for 200min, filtering, and drying the obtained solid substance at 190 ℃ for 20h to obtain the iron lanthanum oxide molecular sieve type purification material.
2. The method for preparing iron lanthanum oxide molecular sieve type purification material according to claim 1, wherein the prepared iron lanthanum oxide molecular sieve type purification material has the following technical characteristics: pore size is 6-7 nm, and specific surface area is 520-760 m2Per g, pore volume of 0.5-0.6 cm3(ii) a bulk density of 0.9 to 1.0g/cm3
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