CN116116383A - Black talcum-based composite air purifying agent and preparation method thereof - Google Patents
Black talcum-based composite air purifying agent and preparation method thereof Download PDFInfo
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- CN116116383A CN116116383A CN202211445597.1A CN202211445597A CN116116383A CN 116116383 A CN116116383 A CN 116116383A CN 202211445597 A CN202211445597 A CN 202211445597A CN 116116383 A CN116116383 A CN 116116383A
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- 239000000454 talc Substances 0.000 title claims abstract description 60
- 229910052623 talc Inorganic materials 0.000 title claims abstract description 60
- 235000012222 talc Nutrition 0.000 title claims abstract description 60
- 239000002131 composite material Substances 0.000 title claims abstract description 21
- 239000012629 purifying agent Substances 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title abstract description 11
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 15
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000010457 zeolite Substances 0.000 claims abstract description 15
- 238000005530 etching Methods 0.000 claims abstract description 8
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 63
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 claims description 52
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 21
- 238000000227 grinding Methods 0.000 claims description 20
- 239000008367 deionised water Substances 0.000 claims description 19
- 229910021641 deionized water Inorganic materials 0.000 claims description 19
- 238000007873 sieving Methods 0.000 claims description 18
- 238000001035 drying Methods 0.000 claims description 17
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 15
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 235000019441 ethanol Nutrition 0.000 claims description 14
- 229910052680 mordenite Inorganic materials 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 13
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 9
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 8
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 8
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 8
- 239000003960 organic solvent Substances 0.000 claims description 8
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 8
- 239000000843 powder Substances 0.000 claims description 8
- 239000011230 binding agent Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 6
- 239000012295 chemical reaction liquid Substances 0.000 claims description 5
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 3
- 235000017550 sodium carbonate Nutrition 0.000 claims description 3
- WYTZZXDRDKSJID-UHFFFAOYSA-N (3-aminopropyl)triethoxysilane Chemical compound CCO[Si](OCC)(OCC)CCCN WYTZZXDRDKSJID-UHFFFAOYSA-N 0.000 claims description 2
- UUEWCQRISZBELL-UHFFFAOYSA-N 3-trimethoxysilylpropane-1-thiol Chemical compound CO[Si](OC)(OC)CCCS UUEWCQRISZBELL-UHFFFAOYSA-N 0.000 claims description 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 2
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 2
- 239000000908 ammonium hydroxide Substances 0.000 claims description 2
- 239000011736 potassium bicarbonate Substances 0.000 claims description 2
- 235000015497 potassium bicarbonate Nutrition 0.000 claims description 2
- 229910000028 potassium bicarbonate Inorganic materials 0.000 claims description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 2
- 235000011181 potassium carbonates Nutrition 0.000 claims description 2
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 claims description 2
- 235000011118 potassium hydroxide Nutrition 0.000 claims description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims 2
- MTEZSDOQASFMDI-UHFFFAOYSA-N 1-trimethoxysilylpropan-1-ol Chemical compound CCC(O)[Si](OC)(OC)OC MTEZSDOQASFMDI-UHFFFAOYSA-N 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 8
- 238000000498 ball milling Methods 0.000 abstract description 7
- 239000003463 adsorbent Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 3
- 239000011707 mineral Substances 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000013329 compounding Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 125000000524 functional group Chemical group 0.000 abstract description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 abstract description 2
- 239000004005 microsphere Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 6
- 239000012798 spherical particle Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- -1 papermaking Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- HVBSAKJJOYLTQU-UHFFFAOYSA-N 4-aminobenzenesulfonic acid Chemical compound NC1=CC=C(S(O)(=O)=O)C=C1 HVBSAKJJOYLTQU-UHFFFAOYSA-N 0.000 description 1
- LSMQKPQSDSZFEZ-UHFFFAOYSA-N C=O.[C] Chemical class C=O.[C] LSMQKPQSDSZFEZ-UHFFFAOYSA-N 0.000 description 1
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000004312 hexamethylene tetramine Substances 0.000 description 1
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 229950000244 sulfanilic acid Drugs 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- BPSIOYPQMFLKFR-UHFFFAOYSA-N trimethoxy-[3-(oxiran-2-ylmethoxy)propyl]silane Chemical compound CO[Si](OC)(OC)CCCOCC1CO1 BPSIOYPQMFLKFR-UHFFFAOYSA-N 0.000 description 1
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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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/02—Separation 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
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/16—Alumino-silicates
- B01J20/18—Synthetic zeolitic molecular sieves
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
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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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
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- B01J20/2803—Sorbents comprising a binder, e.g. for forming aggregated, agglomerated or granulated products
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Abstract
The invention discloses a black talcum-based composite air purifying agent and a preparation method thereof, belonging to the field of comprehensive utilization of nonmetallic minerals. The method comprises the following steps: and etching the black talcum after ball milling to increase the specific surface area and the porosity of the black talcum, so that the surface of the black talcum is rich in active functional groups, then grafting, grafting active groups to increase the adsorption quantity of formaldehyde, and finally compounding and granulating with mercerized zeolite to obtain the small microsphere. The advantages of the graphene-like layer, the lamellar structure and the like of the black talcum are effectively utilized. The preparation process is simple, the raw materials are cheap and easy to obtain, the adsorption effect is good, the production scale is easy to control, the environment is protected, and no secondary pollution is generated. The invention provides a new direction for the production field of the adsorbent, reduces the cost of the existing adsorbent, and provides an effective, economical and practical way for improving the comprehensive utilization of the black talc ore.
Description
Technical Field
The invention belongs to the field of comprehensive utilization of nonmetallic minerals, and particularly relates to a black talc-based composite air purifying agent and a preparation method thereof.
Background
The most main indoor pollution source is formaldehyde, and the national sanitation standard prescribes that the indoor formaldehyde concentration is not more than 0.08mg/m 3 Especially in the room after the fitment, formaldehyde concentration seriously exceeds standard, brings very big influence to human health, and the commercial formaldehyde adsorbent of present stage is the active carbon package almost, but active carbon package adsorption capacity is less, is difficult to regenerate for remove formaldehyde thoroughly, still has the problem of with high costs.
The black smooth stone ore has black color, purer chemical composition, fine particles, flaky structure, higher specific surface area, no asbestos harmful minerals, huge reserve, lower exploitation cost and low price, and is widely used in industrial products such as ceramics, papermaking, fillers and the like. The vast majority of the black talc products are low-end products such as fillers, and there is still a great development space in other high-end technology fields. The properties of the black talc can be reasonably utilized for modification, and the performance of the black talc in other aspects is improved. The technology not only accords with the novel industrial road and sustainable development strategy in China, but also widens the application field of the black talc and increases the economic benefit brought by the black talc industry.
Disclosure of Invention
Aiming at the problems of higher development cost and lower adsorption capacity of the existing activated carbon formaldehyde adsorbent, the invention provides a preparation method of a black talc-based composite air purifying agent. The air purifying agent is synthesized through steps of etching, grafting, compounding and the like, has simple operation process, good adsorption effect on formaldehyde and other air polar pollutants, and has high recovery efficiency.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
the invention provides a black talc-based composite air purifying agent, which is prepared by the following steps:
(1) Etching of black talc: immersing black talc powder with the average particle size of 200-500 nm (preferably 300-400 nm) into an aqueous solution of alkaline substances with the total concentration of 1-4 mol/L (preferably 2 mol/L), heating and stirring at 60-90 ℃ for 6-10 hours (preferably 70 ℃ for 7 hours), and carrying out post-treatment A on the obtained reaction solution A to obtain etched black talc powder; the alkaline substance in the aqueous solution of the alkaline substance is one or more than two of sodium hydroxide, potassium hydroxide, sodium carbonate, sodium bicarbonate, potassium carbonate, potassium bicarbonate and ammonium hydroxide (ammonia water).
The etching aims to etch part of silicon between the lamellar layers of the black talc, so that the pore channel structure of the black talc is more abundant, and the surface of the black talc is rich in active functional groups.
(2) Adding the etched black talcum powder obtained in the step (1) into an organic solvent, adding a grafting agent, carrying out grafting reaction for 3-8 hours (preferably 5 hours) at 50-90 ℃ (preferably 70 ℃), and carrying out post-treatment on the obtained reaction liquid B to obtain grafted black talcum powder; the grafting agent is one or more than two of N-beta- (aminoethyl) -gamma-aminopropyl trimethoxysilane (KH 792), gamma-aminopropyl triethoxysilane (KH 550), gamma-glycidoxypropyl trimethoxysilane (KH 560) and gamma-mercaptopropyl trimethoxysilane (KH 590) (preferably N-beta- (aminoethyl) -gamma-aminopropyl trimethoxysilane); the mass ratio of the grafting agent to the etched black talcum powder is 1:1-3 (preferably 1:1);
the grafting aims to graft hydroxyl rich on the surface of the black talcum, and the grafting is carried out with active groups so as to increase the adsorption quantity of formaldehyde.
(3) The grafted black talcum powder, mercerized zeolite powder with the average particle diameter of 200-500 nm (preferably 300-400 nm) and the binder are mixed and granulated to obtain the black talcum-based composite air purifying agent; the mass ratio of the grafted black talcum powder to the mordenite to the binder is 1:0.5 to 3:0.2 to 0.5 (preferably 1:1:0.33).
Further, the volume of the aqueous solution of the alkaline substance in the step (1) is 1 to 5mL/g (2.5 mL/g) based on the mass of the black talc powder.
Further, the post-treatment in step (1) is: the reaction solution was cooled to room temperature, centrifuged (in one embodiment of the invention, 5000rpm/min for 5 min), and the obtained precipitate was centrifugally washed with deionized water to neutrality, dried, and sieved (200 mesh) to obtain etched black talc powder.
Further, the organic solvent in the step (2) is one or more of toluene, ethanol, methanol, and acetone (preferably, one or more of methanol and toluene, and most preferably, toluene).
Preferably, the volume of the organic solvent in the step (2) is 1 to 5ml/g (3 ml/g) based on the mass of the etched black talc powder.
Further, the post-treatment B in step (2) is: and (3) cooling the reaction liquid B, centrifuging, re-suspending and washing the obtained precipitate with absolute ethyl alcohol for three times, drying the obtained lower layer solid (60 ℃), grinding and sieving (200 meshes) to obtain the grafted black talcum powder.
Further, the binder in the step (3) is one or a mixture of more than two of polyvinyl alcohol (PVA), sodium carbonate and ethyl orthosilicate (preferably polyvinyl alcohol).
In one embodiment of the invention, the speed of rotation of the granulation in step (3) is 32r/min, resulting in spherical particles with a diameter of 2-3 mm. The rotating speed can be set according to the requirement in actual production.
The invention provides a black talc powder having an average particle diameter of 200 to 500nm (preferably 300 to 400 nm) in the step (1), which is prepared by the following method: crushing, grinding and sieving black talc (200 meshes) in Guangfeng region of Shangshi, jiangxi province to obtain black talc powder, adding ethanol and deionized water into the black talc powder, ball milling in a ball mill by a wet method, taking out a sample, re-suspending and washing with deionized water, taking out the solid at the lower layer in a centrifuge tube, drying, grinding and sieving (200 meshes) to obtain superfine black talc powder with the average particle diameter of 200-500 nm; the volume ratio of the ethanol to the deionized water is 0.5-2:1 (preferably 1:1); the total volume of ethanol and deionized water is based on complete immersion of the black talc powder. Preferably, the volume of the ethanol is 0.6-1.6mL/g based on the mass of the black talc powder. The rotational speed of the wet ball milling is 700-800 r/min, and the time is 8-10 h. The drying temperature is 60-120 ℃ (preferably 80-100 ℃) and the drying time is 12-15 hours.
The invention provides a mercerized zeolite powder with the average grain diameter of 200-500 nm (preferably 300-400 nm) in the step (3), which is prepared by the following method: crushing mordenite (Jiangsu Jinyun), grinding, sieving (200 meshes) to obtain mordenite powder, adding ethanol and deionized water into the mordenite powder, performing wet ball milling in a ball mill, taking out a sample, performing deionized water resuspension washing, taking out the lower solid in a centrifuge tube, drying, grinding and sieving (200 meshes) to obtain superfine mordenite powder, wherein the average particle size of the superfine mordenite powder is 200-500 nm; the volume ratio of the ethanol to the deionized water is 0.5-2:1 (preferably 1:1); the total volume of ethanol and deionized water is based on complete immersion of the black talc powder. Preferably the volume of ethanol is from 0.6 to 1.6mL/g based on the mass of the mordenite powder. The rotational speed of the wet ball milling is 700-800 r/min, and the time is 8-10 h. The drying temperature is 60-120 ℃ (preferably 80-100 ℃) and the drying time is 12-15 hours.
The invention also provides application of the black talc-based composite air purifying agent in formaldehyde adsorption.
Compared with the existing materials, the invention has the beneficial effects that: the black talc is ball-milled, the specific surface area of the black talc is effectively increased, the black talc is etched, the surface is rich in active groups, the specific surface area is further increased, pore channels are enriched, the grafting activation is carried out, the structure of a graphene-like layer is reserved, the active groups are rich on the surface, and finally the mercerized zeolite with high adsorption capacity is compounded, so that the adsorption capacity of formaldehyde is greatly increased. The preparation process is simple, the raw materials are cheap and easy to obtain, the production scale is easy to control, the environment is protected, and no secondary pollution is generated. The invention provides a new direction for the field of black talcum adsorbents, and simultaneously provides an effective, economical and practical way for improving the comprehensive utilization of the black talcum ores.
Drawings
FIG. 1 FT-IR chart of the black talc before and after grafting in example 1.
Detailed Description
The present invention will be further described with reference to specific examples, but the present invention is not limited to the following examples, and various modifications are intended to be included within the technical scope of the present invention without departing from the spirit and scope of the present invention.
The formaldehyde testing method comprises the following steps: placing formaldehyde detector (kanfar JQ151 type) in a sealed glass container with dimensions of 30cm×30cm, introducing formaldehyde into the sealed chamber, and ensuring formaldehyde concentration at 0.5mg/m 3 Then 50g of adsorbent particles are put into the mixture for adsorption, the reading of a formaldehyde detector is observed after 5 hours, and the formaldehyde adsorption rate is calculated. A blank is placed.
Example 1
(1) The following conditions for preparing the black talc powder were: taking black talcum from Guangfeng of Jiangxi, crushing, grinding, sieving (200 meshes) to obtain black talcum powder, adding 80ml of ethanol and 80ml of deionized water into 100g of black talcum powder, placing into a ball mill, grinding by a wet method at a rotating speed of 800r/min for 10 hours, taking out a sample, re-suspending and washing by the deionized water, centrifuging for three times, taking out the solid at the lower layer in a centrifuge tube, drying at 80 ℃ for 12 hours, grinding and sieving (200 meshes) to obtain superfine black talcum powder, wherein the average particle size of the superfine black talcum powder is 300nm.
(2) Etching of black talc: taking 80g of the superfine black talc powder in the step (1), heating and stirring in a water bath of 70 ℃ in 200ml of 2mol/L NaOH solution for 7h, cooling to room temperature, centrifuging at 5000rpm/min for 5min, re-suspending and washing with deionized water until the supernatant is neutral, drying, grinding and sieving (200 meshes) to obtain etched black talc powder;
(3) Preparation of grafted black talc: placing 80g of etched black talc in the step (2) in 240ml of toluene, adding 80g of KH792, placing in a reaction kettle, heating at 70 ℃ for 5 hours, cooling, centrifuging to remove the lower layer solid, adding absolute ethyl alcohol, carrying out resuspension washing, centrifuging, repeating for three times, removing the lower layer solid, drying at 60 ℃, taking out, grinding and sieving (200 meshes) to obtain grafted black talc.
(4) Preparation of mordenite: selecting a Jinyun zeolite ore produced in Jiangsu, yun, crushing, and ball-milling in the mode of the step (1), wherein the average grain size is 300nm.
(5) Black talc based composite air cleaner: 30g of grafted black talcum powder, 30g of mordenite and 10g of PVA are taken and granulated in a disc granulator at the speed of 32r/min, so as to obtain spherical particles with the diameter of 2-3 mm. Wherein the mercerized Jinyun zeolite is formed by crushing Jinyun zeolite ore.
(6) The formaldehyde removal rate of the obtained product is 97.8%.
Example 2
The other operations were the same as in example 1, except that the grafting agent in step (3) was different in kind and the other conditions were the same. The grafting agent species used are listed in the table below.
Name of the name | Formaldehyde adsorption rate (%) |
80g KH550 | 96.0 |
80g KH560 | 91.2 |
80g KH590 | 93.5 |
80g of triethanolamine | 86.2 |
80g of p-aminobenzenesulfonic acid | 89.5 |
80g of hexamethylenetetramine | 81.3 |
Example 3
The other operations were the same as in example 1, except that the binder type in step (5) was different, and the other conditions were the same. The grafting agent species used are listed in the table below.
Example 4
The other operations were identical to example 1, except that the mass ratio of black talc to mordenite in step (5) was different, all other conditions being identical. The grafting agent species used are listed in the table below.
Example 5
The other operations were the same as in example 1, except that the organic solvent in step (3) was different in kind and the other conditions were the same. The grafting agent species used are listed in the table below.
Name of the name | Formaldehyde adsorption rate (%) |
240ml of ethanol | 87.1 |
240ml of methanol | 90.2 |
240ml of acetone | 86.4 |
Comparative example 1
(1) The following conditions for preparing the black talc powder were: taking black talcum from Guangfeng of Jiangxi, crushing, grinding, sieving (200 meshes) to obtain black talcum powder, adding 80ml of ethanol and 80ml of deionized water into 100g of black talcum powder, placing into a ball mill, grinding by a wet method at a rotating speed of 800r/min for 10 hours, taking out a sample, re-suspending and washing by the deionized water, centrifuging for three times, taking out the solid at the lower layer in a centrifuge tube, drying at 80 ℃ for 12 hours, grinding and sieving (200 meshes) to obtain superfine black talcum powder, wherein the average particle size of the superfine black talcum powder is 300nm.
(2) Etching of black talc: taking 80g of the superfine black talc powder in the step (1), heating and stirring in a water bath of 70 ℃ in 200ml of 2mol/L NaOH solution for 7h, cooling to room temperature, centrifuging at 5000rpm/min for 5min, re-suspending and washing with deionized water until the supernatant is neutral, drying, grinding and sieving (200 meshes) to obtain etched black talc powder;
(3) Preparation of grafted black talc: and (3) placing 80g of etched black talc in the step (2) in 240ml of toluene, adding 80g of KH792, placing in a reaction kettle, heating at 70 ℃ for 5 hours, cooling, centrifuging to remove the lower layer solid, adding absolute ethyl alcohol, re-suspending, washing, centrifuging, repeating for three times, taking the lower layer solid, drying at 60 ℃, taking out, grinding and sieving (200 meshes) to obtain grafted black talc.
(4) Black talc based air cleaner: 60g of grafted black talc and 10g of PVA are granulated in a granulator to obtain spherical particles with diameters of 2-3 mm.
(5) The formaldehyde removal rate of the obtained product is 62%.
Comparative example 2
(1) Mordenite zeolite: 60g of mercerized Jinyun zeolite and 10g of PVA are taken out in a granulator for granulation, and spherical particles with the diameter of 2-3 mm are obtained.
(2) The formaldehyde removal rate of the obtained product is 40%.
Comparative example 3
(1) The following conditions for preparing the black talc powder were: taking black talcum from Guangfeng of Jiangxi, crushing, grinding, sieving (200 meshes) to obtain black talcum powder, adding 80ml of ethanol and 80ml of deionized water into 100g of black talcum powder, placing into a ball mill, grinding by a wet method at a rotating speed of 800r/min for 10 hours, taking out a sample, re-suspending and washing by the deionized water, centrifuging for three times, taking out the solid at the lower layer in a centrifuge tube, drying at 80 ℃ for 12 hours, grinding and sieving (200 meshes) to obtain superfine black talcum powder, wherein the average particle size of the superfine black talcum powder is 300nm.
(2) Etching of black talc: taking 80g of the superfine black talc powder in the step (1), heating and stirring in a water bath of 70 ℃ in 200ml of 2mol/L NaOH solution for 7h, cooling to room temperature, centrifuging at 5000rpm/min for 5min, re-suspending and washing with deionized water until the supernatant is neutral, drying, grinding and sieving (200 meshes) to obtain etched black talc powder;
(3) Preparation of mordenite: selecting and crushing a Jinyun zeolite ore produced in Jiangsu, and ball-milling in the mode of the step (1), wherein the particle size of the Jinyun zeolite ore is the same as that of the black talc.
(4) Black talc based composite air cleaner: 30g of black talcum powder, 30g of mordenite zeolite and 10g of PVA are taken and granulated in a disc granulator at the speed of 32r/min, so as to obtain spherical particles with the diameter of 2-3 mm. Wherein the mercerized Jinyun zeolite is formed by crushing Jinyun zeolite ore.
(5) The formaldehyde removal rate of the obtained product is 73.7%.
Claims (10)
1. The black talc-based composite air purifying agent is characterized by being prepared by the following steps:
(1) Etching of black talc: immersing black talcum powder with the average grain diameter of 200-500 nm into an aqueous solution of alkaline substances with the total concentration of 1-4 mol/L, heating and stirring at 60-90 ℃ for 6-10 hours, and carrying out post-treatment A on the obtained reaction solution A to obtain etched black talcum powder; the alkaline substance in the aqueous solution of the alkaline substance is one or more than two of sodium hydroxide, potassium hydroxide, sodium carbonate, sodium bicarbonate, potassium carbonate, potassium bicarbonate and ammonium hydroxide.
(2) Adding the etched black talcum powder obtained in the step (1) into an organic solvent, adding a grafting agent, and carrying out grafting reaction for 3-8 hours at 50-90 ℃, wherein the obtained reaction liquid B is subjected to post-treatment B to obtain grafted black talcum powder; the grafting agent is one or more than two of N-beta- (aminoethyl) -gamma-aminopropyl trimethoxysilane, gamma-aminopropyl triethoxysilane, gamma-glycidol ether oxypropyl trimethoxysilane and gamma-mercaptopropyl trimethoxysilane; the mass ratio of the grafting agent to the etched black talcum powder is 1:1-3;
(3) The grafted black talcum powder, mercerized zeolite powder with the average grain diameter of 200-500 nm and the binder are mixed and granulated to obtain the black talcum-based composite air purifying agent; the mass ratio of the grafted black talcum powder to the mordenite to the binder is 1:0.5 to 3:0.2 to 0.5.
2. The black talc-based composite air purifying agent according to claim 1, wherein: the volume of the aqueous solution of the alkaline substance in the step (1) is 1 to 5mL/g based on the mass of the black talc powder.
3. The black talc-based composite air purifying agent according to claim 1, wherein: the post-treatment in the step (1) is as follows: and cooling the reaction liquid to room temperature, centrifuging, centrifugally washing the obtained precipitate with deionized water to neutrality, drying, and sieving to obtain etched black talcum powder.
4. The black talc-based composite air purifying agent according to claim 1, wherein: the grafting agent in the step (2) is N-beta- (aminoethyl) -gamma-aminopropyl trimethoxysilane.
5. The black talc-based composite air purifying agent according to claim 1, wherein: the organic solvent in the step (2) is one or a mixture of more than two of toluene, ethanol, methanol and acetone.
6. The black talc-based composite air purifying agent according to claim 1, wherein: the organic solvent in the step (2) is one or a mixture of more than two of methanol and toluene.
7. The black talc-based composite air purifying agent according to claim 1, wherein: the volume of the organic solvent in the step (2) is 1-5 ml/g based on the mass of the etched black talcum powder.
8. The black talc-based composite air purifying agent according to claim 1, wherein: the post-treatment B in the step (2) is as follows: and (3) cooling the reaction liquid B, centrifuging, re-suspending and washing the obtained precipitate with absolute ethyl alcohol for three times, drying the obtained lower layer solid, grinding and sieving to obtain the grafted black talcum powder.
9. The black talc-based composite air purifying agent according to claim 1, wherein: the binder in the step (3) is one or a mixture of more than two of polyvinyl alcohol, sodium carbonate and tetraethoxysilane.
10. Use of the black talc based composite air cleaner according to claim 1 for adsorbing formaldehyde.
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CN103084144A (en) * | 2013-02-06 | 2013-05-08 | 中国科学院广州地球化学研究所 | Diatomite-based porous composite material for adsorbing volatile organic pollutants and preparation method thereof |
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CN114989494A (en) * | 2022-06-30 | 2022-09-02 | 中国地质大学(武汉) | Modified black talc antibacterial material and dry preparation process and application thereof |
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JP2009136832A (en) * | 2007-12-10 | 2009-06-25 | National Institute Of Advanced Industrial & Technology | Natural mineral membrane |
CN101254924A (en) * | 2008-04-09 | 2008-09-03 | 中国科学院化学研究所 | Silicane coupling agent surface grafted modified clay as well as preparation method and use thereof |
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