CN112624166A - Preparation method of silicon-aluminum-based aerogel and application of prepared silicon-aluminum-based aerogel in aspect of adsorbing heavy metal gas - Google Patents
Preparation method of silicon-aluminum-based aerogel and application of prepared silicon-aluminum-based aerogel in aspect of adsorbing heavy metal gas Download PDFInfo
- Publication number
- CN112624166A CN112624166A CN202011492751.1A CN202011492751A CN112624166A CN 112624166 A CN112624166 A CN 112624166A CN 202011492751 A CN202011492751 A CN 202011492751A CN 112624166 A CN112624166 A CN 112624166A
- Authority
- CN
- China
- Prior art keywords
- aluminum
- silicon
- based aerogel
- aerogel
- solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000004964 aerogel Substances 0.000 title claims abstract description 91
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 229910001385 heavy metal Inorganic materials 0.000 title claims description 36
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 72
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000003756 stirring Methods 0.000 claims abstract description 36
- 239000000243 solution Substances 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000000463 material Substances 0.000 claims abstract description 27
- 238000002156 mixing Methods 0.000 claims abstract description 25
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000011259 mixed solution Substances 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims abstract description 19
- 239000002243 precursor Substances 0.000 claims abstract description 19
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000002904 solvent Substances 0.000 claims abstract description 15
- 238000001035 drying Methods 0.000 claims abstract description 14
- 239000011240 wet gel Substances 0.000 claims abstract description 12
- 230000007935 neutral effect Effects 0.000 claims abstract description 9
- 238000001291 vacuum drying Methods 0.000 claims abstract description 9
- 230000002378 acidificating effect Effects 0.000 claims abstract description 6
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims abstract description 4
- 238000001816 cooling Methods 0.000 claims abstract description 3
- 238000010992 reflux Methods 0.000 claims abstract description 3
- 238000001179 sorption measurement Methods 0.000 claims description 45
- 239000007789 gas Substances 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 18
- 238000000197 pyrolysis Methods 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical group Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 25
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 17
- 238000002474 experimental method Methods 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 239000011148 porous material Substances 0.000 description 8
- 229910052782 aluminium Inorganic materials 0.000 description 7
- 229910052710 silicon Inorganic materials 0.000 description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 6
- 244000282866 Euchlaena mexicana Species 0.000 description 6
- 239000003463 adsorbent Substances 0.000 description 6
- 230000032683 aging Effects 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 235000011114 ammonium hydroxide Nutrition 0.000 description 6
- 239000003814 drug Substances 0.000 description 6
- 239000010419 fine particle Substances 0.000 description 6
- 238000000227 grinding Methods 0.000 description 6
- 239000004570 mortar (masonry) Substances 0.000 description 6
- 238000012216 screening Methods 0.000 description 6
- 238000010517 secondary reaction Methods 0.000 description 6
- 239000010703 silicon Substances 0.000 description 6
- 239000000377 silicon dioxide Substances 0.000 description 6
- 239000004965 Silica aerogel Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 4
- 239000002910 solid waste Substances 0.000 description 4
- 229910003439 heavy metal oxide Inorganic materials 0.000 description 3
- 238000001095 inductively coupled plasma mass spectrometry Methods 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- 229910020662 PbSiO3 Inorganic materials 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910052681 coesite Inorganic materials 0.000 description 2
- 229910052906 cristobalite Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- HWSZZLVAJGOAAY-UHFFFAOYSA-L lead(II) chloride Chemical compound Cl[Pb]Cl HWSZZLVAJGOAAY-UHFFFAOYSA-L 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 229910052682 stishovite Inorganic materials 0.000 description 2
- 229910052905 tridymite Inorganic materials 0.000 description 2
- 239000005995 Aluminium silicate Substances 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 229960000892 attapulgite Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000000411 inducer Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052625 palygorskite Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
-
- 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
- B01J20/06—Solid 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
- B01J20/08—Solid 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 comprising aluminium oxide or hydroxide; comprising bauxite
-
- 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
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
-
- 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
- B01J20/28014—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
- B01J20/28047—Gels
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/157—After-treatment of gels
- C01B33/158—Purification; Drying; Dehydrating
- C01B33/1585—Dehydration into aerogels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/60—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/80—Particles consisting of a mixture of two or more inorganic phases
- C01P2004/82—Particles consisting of a mixture of two or more inorganic phases two phases having the same anion, e.g. both oxidic phases
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/14—Pore volume
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Silicon Compounds (AREA)
Abstract
The invention discloses a preparation method of silicon-aluminum based aerogel, which comprises the following steps: (1) adding aluminum isopropoxide into a mixed solution of ethanol and water to obtain a mixed material, heating and refluxing the mixed material under a stirring condition, stopping stirring, continuing heating, cooling to room temperature after heating, and adjusting the pH value of the solution to make the solution acidic to obtain alumina wet sol; (2) adding tetraethoxysilane into a mixed solution of ethanol and water, stirring, and adjusting the pH value of the solution to make the solution acidic to obtain a silica sol precursor solution; (3) and (3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), adjusting the pH value of the mixed solution to be neutral after stirring, standing the mixed solution for at least 12 hours to form silicon-aluminum wet gel, performing solvent exchange by using n-hexane, and drying the silicon-aluminum wet gel in a vacuum drying oven to obtain the silicon-aluminum-based aerogel.
Description
Technical Field
The invention relates to a preparation method of a silicon-aluminum based aerogel and also relates to application of the silicon-aluminum based aerogel prepared by the preparation method in the aspect of adsorbing heavy metal gas.
Background
Solid wastes generated in human production and life severely pollute water and soil in the nature. Pyrolysis technology is generally employed to render solid waste harmless. However, in the process of pyrolyzing solid waste, especially in the process of pyrolyzing solid waste containing chlorine element, volatile and semi-volatile heavy metals can be easily volatilized to the external environment in the form of chloride, thereby causing secondary pollution to the environment. Therefore, a material capable of efficiently adsorbing heavy metal gas is required to be found. At present, the materials for adsorbing the heavy metal gases are mainly natural raw materials rich in Si and Al, such as kaolin, attapulgite, limestone and the like. However, these materials often occur on the surface of the adsorbent when adsorbing and solidifying heavy metal gas, and cannot permeate into the interior of the adsorbent, resulting in low utilization rate of the adsorbent.
In recent years, silica aerogel has been receiving more and more attention due to its unique pore structure. The silica aerogel has larger specific surface area and porosity, can adsorb and contain more particles, and is favorable for being applied to the adsorption of heavy metal gas in the pyrolysis process. However, the silicon dioxide aerogel has poor thermal stability, and the pore channel is easy to collapse at high temperature, so that the structure is densified, and the silicon dioxide aerogel cannot be applied to heavy metal gas adsorption in the actual high-temperature pyrolysis process.
Disclosure of Invention
The purpose of the invention is as follows: aiming at the problem that the silicon dioxide aerogel in the prior art cannot adsorb heavy metal gas in the high-temperature pyrolysis process, the invention provides the preparation method of the silicon-aluminum-based aerogel.
The technical scheme is as follows: the preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) adding aluminum isopropoxide into a mixed solution of ethanol and water to obtain a mixed material, heating and refluxing the mixed material under a stirring condition, continuing to heat after stirring is stopped, cooling to room temperature after heating, and adjusting the pH value of the solution to be acidic to obtain alumina wet sol;
(2) adding tetraethoxysilane into a mixed solution of ethanol and water, stirring for no more than 0.5h, and adjusting the pH value of the solution to be acidic to obtain a silica sol precursor solution;
(3) and (3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), adjusting the pH value of the mixed solution to be neutral after stirring, standing the mixed solution for at least 12 hours to form silicon-aluminum mixed wet gel, performing solvent exchange by using n-hexane, and drying the silicon-aluminum mixed wet gel in a vacuum drying oven to obtain the silicon-aluminum-based aerogel.
Wherein in the step (1), the mixing volume ratio of the ethanol and the water is 15-30: 5-10.
Wherein in the step (2), the mixing molar ratio of the ethanol to the water is 5-7: 1-3.
Wherein, in the step (3), the drying temperature is 50-60 ℃, and the drying time is 6-10 h.
Wherein, in the step (3), the molar ratio of silicon-aluminum elements in the obtained silicon-aluminum based aerogel is 1: 1.
The silicon-aluminum-based aerogel prepared by the preparation method of the silicon-aluminum-based aerogel is applied to the aspect of adsorbing heavy metal gas.
The silicon-aluminum-based aerogel is used for adsorbing heavy metal gas in the pyrolysis process, and the temperature of the pyrolysis process is 600-900 ℃.
The silicon-aluminum based aerogel prepared by the invention has large specific surface area and poresThe porosity enables heavy metal gas to enter the pore channels of the aerogel material, so that the utilization rate of the material is improved, and meanwhile, the effect of solidifying heavy metal can be well played, so that the heavy metal adsorption efficiency is improved; the silicon-aluminum based aerogel contains rich Si element and can form silicate with heavy metal oxide; meanwhile, aiming at heavy metal chloride, alumina in the silicon-aluminum-based aerogel can react with chloride in heavy metal gas to generate heavy metal oxide, and then the heavy metal oxide continuously reacts with silica in the aerogel to generate silicate, specifically, a part of heavy metal chloride can be fixed inside the pore channel of the silicon-aluminum-based aerogel in a physical adsorption mode, and the other part of heavy metal chloride forms stable silicate with the silicon-aluminum-based aerogel, so that the adsorption efficiency and the utilization rate of the aerogel material are improved, (such as PbCl for example)2The reaction mechanism is as follows: PbCl2+SiO2+H2O＝PbSiO3+2HCl；3PbCl2+Al2O3＝2AlCl3+3PbO，PbO+SiO2＝PbSiO3)。
Has the advantages that: the preparation method has simple process, can also obtain the alumina sol without using an inducer and a catalyst, and then obtains the silica sol precursor solution by controlling the hydrolysis time of the tetraethoxysilane and the pH value of the reaction solution; the silicon-aluminum based aerogel prepared by the invention has high thermal stability, large specific surface area and porosity, and can keep a stable pore structure at 500-900 ℃, so that the silicon-aluminum based aerogel can be used for adsorbing heavy metal gas in the pyrolysis process.
Drawings
FIG. 1 shows the silica-alumina based aerogels prepared in examples 1 to 6 as a heavy metal gas PbCl2Comparative adsorption performance of (c).
Detailed Description
The technical solution of the present invention is further described with reference to the following specific embodiments.
Example 1
The preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) 2.5g of Aluminum Isopropoxide (AIP) was added to a mixed solution of ethanol and water in a mixed volume ratio of 15 mL: 5mL of the alumina wet sol is mixed, heated and refluxed for 3 hours at the temperature of 80 ℃ under the stirring condition, the stirring is stopped, the heating is continued for 1 hour, the mixture is cooled to the room temperature, hydrochloric acid is added to adjust the pH value to be 3, and the mixture is stirred for 10min to obtain the alumina wet sol;
(2) adding 2.55g of TEOS into a mixed solution of ethanol and water, wherein the mixing molar ratio of the ethanol to the water is 7: 3, mixing and stirring for 0.5h (silica sol cannot be formed in a short treatment time), and then adjusting the pH value to 2 by using hydrochloric acid to obtain a silica sol precursor solution;
(3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), stirring for 2 hours, adding ammonia water to adjust the pH value to be neutral, standing for 12 hours to form a silicon-aluminum mixed wet gel, exchanging an ethanol solvent with n-hexane without heating and aging, performing solvent exchange with n-hexane (changing the structure of the material by changing the polarity of the solution), and drying in a vacuum drying oven at 50 ℃ for 6 hours to obtain the silicon-aluminum based aerogel (the molar ratio of silicon to aluminum in the silicon-aluminum based aerogel is 1: 1); and grinding the dried silicon-aluminum-based aerogel into fine particles by using a mortar, and screening materials with the size of 40-60 meshes by using a medicine screen to perform an adsorption experiment.
The specific surface area of the silica-alumina-based aerogel prepared in example 1 was 686.22m2·g-1Porosity of 0.57cm3·g-1。
0.6g of silica-alumina aerogel is weighed, and 0.06g of PbCl is weighed2Adding into a secondary reaction furnace for PbCl2And (4) performing gas adsorption experiments. Adsorbing at 800 deg.C for 40min with PbCl2The adsorption removal rate of the silica-alumina-based aerogel is 72.58%, which shows that the silica-alumina-based aerogel prepared in example 1 has good heavy metal gas adsorption performance.
Example 2
The preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) 2.5g of Aluminum Isopropoxide (AIP) was added to a mixed solution of ethanol and water in a mixed volume ratio of 15 mL: 5mL of the alumina wet sol is mixed, heated and refluxed for 3 hours at the temperature of 80 ℃ under the stirring condition, the stirring is stopped, the heating is continued for 1 hour, the mixture is cooled to the room temperature, hydrochloric acid is added to adjust the pH value to be 3, and the mixture is stirred for 10min to obtain the alumina wet sol;
(2) adding 2.55g of TEOS into a mixed solution of ethanol and water, wherein the mixing molar ratio of the ethanol to the water is 7: 3, mixing and stirring for 0.5h (no silica sol is formed in a short treatment time), and then adjusting the pH value to 2 by using hydrochloric acid to obtain a silica sol precursor solution;
(3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), stirring for 2 hours, adding ammonia water to adjust the pH value to be neutral, standing for 12 hours to form a silicon-aluminum mixed wet gel, exchanging an ethanol solvent with n-hexane without heating and aging, performing solvent exchange with n-hexane (changing the structure of the material by changing the polarity of the solution), and drying in a vacuum drying oven at 60 ℃ for 10 hours to obtain the silicon-aluminum based aerogel (the molar ratio of silicon to aluminum in the silicon-aluminum based aerogel is 1: 1); and grinding the dried silicon-aluminum-based aerogel into fine particles by using a mortar, and screening materials with the size of 40-60 meshes by using a medicine screen to perform an adsorption experiment.
0.6g of silica-alumina aerogel is weighed, and 0.06g of PbCl is weighed2Adding into a secondary reaction furnace for PbCl2And (4) performing gas adsorption experiments. Adsorbing at 800 deg.C for 40min with PbCl2The adsorption removal rate of (a) was 71.11%, indicating that the drying temperature and time had little effect on the adsorption efficiency.
Example 3
The preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) 2.5g of Aluminum Isopropoxide (AIP) was added to a mixed solution of ethanol and water in a mixed volume ratio of 30 mL: 10mL of the alumina wet sol is mixed, heated and refluxed for 3 hours at 80 ℃ under the stirring condition, the stirring is stopped, the heating is continued for 1 hour, the mixture is cooled to the room temperature, hydrochloric acid is added to adjust the pH value to 3, and the mixture is stirred for 10 minutes to obtain the alumina wet sol;
(2) adding 2.55g of TEOS into a mixed solution of ethanol and water, wherein the mixing molar ratio of the ethanol to the water is 7: 3, mixing and stirring for 0.5h (no silica sol is formed in a short treatment time), and then adjusting the pH value to 2 by using hydrochloric acid to obtain a silica sol precursor solution;
(3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), stirring for 2 hours, adding ammonia water to adjust the pH value to be neutral, standing for 12 hours to form a silicon-aluminum mixed wet gel, exchanging an ethanol solvent with n-hexane without heating and aging, performing solvent exchange with n-hexane (changing the structure of the material by changing the polarity of the solution), and drying in a vacuum drying oven at 50 ℃ for 6 hours to obtain the silicon-aluminum based aerogel (the molar ratio of silicon to aluminum in the silicon-aluminum based aerogel is 1: 1); and grinding the dried silicon-aluminum-based aerogel into fine particles by using a mortar, and screening materials with the size of 40-60 meshes by using a medicine screen to perform an adsorption experiment.
0.6g of silica-alumina aerogel is weighed, and 0.06g of PbCl is weighed2Adding into a secondary reaction furnace for PbCl2And (4) performing gas adsorption experiments. Adsorbing at 800 deg.C for 40min with PbCl2The adsorption removal rate of the silica-alumina-based aerogel is 66.54%, which shows that the increase of the ethanol and water content in the step (1) is not beneficial to the adsorption of the silica-alumina-based aerogel on the heavy metal gas, because the aerogel prepared from the ethanol and water with the content has irregular structure, the pore channel is easy to collapse at high temperature, and the structure is densified, so the adsorption performance of the heavy metal gas is reduced.
Example 4
The preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) 2.5g of Aluminum Isopropoxide (AIP) was added to a mixed solution of ethanol and water in a mixed volume ratio of 15 mL: 5mL of the alumina wet sol is mixed, heated and refluxed for 3 hours at the temperature of 80 ℃ under the stirring condition, the stirring is stopped, the heating is continued for 1 hour, the mixture is cooled to the room temperature, hydrochloric acid is added to adjust the pH value to be 3, and the mixture is stirred for 10min to obtain the alumina wet sol;
(2) adding 2.55g of TEOS into a mixed solution of ethanol and water, wherein the mixing molar ratio of the ethanol to the water is 5: 1, mixing and stirring for 0.5h (no silica sol is formed in a short treatment time), and then adjusting the pH value to 2 by using hydrochloric acid to obtain a silica sol precursor solution;
(3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), stirring for 2 hours, adding ammonia water to adjust the pH value to be neutral, standing for 12 hours to form a silicon-aluminum mixed wet gel, exchanging an ethanol solvent with n-hexane without heating and aging, performing solvent exchange with n-hexane (changing the structure of the material by changing the polarity of the solution), and drying in a vacuum drying oven at 50 ℃ for 6 hours to obtain the silicon-aluminum based aerogel (the molar ratio of silicon to aluminum in the silicon-aluminum based aerogel is 1: 1); and grinding the dried silicon-aluminum-based aerogel into fine particles by using a mortar, and screening materials with the size of 40-60 meshes by using a medicine screen to perform an adsorption experiment.
0.6g of silica-alumina aerogel is weighed, and 0.06g of PbCl is weighed2Adding into a secondary reaction furnace for PbCl2And (4) performing gas adsorption experiments. Adsorbing at 800 deg.C for 40min with PbCl2The adsorption removal rate of (3) is 52.31%, which shows that after the alcohol-water ratio in the step (2) is increased, the prepared silicon-aluminum based aerogel is subjected to PbCl2The adsorption efficiency is reduced because the pore structure and the shape of the prepared silica-alumina-based aerogel are not beneficial to the adsorption of heavy metal gas.
Example 5
The preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) 5g of Aluminum Isopropoxide (AIP) was added to a mixed solution of ethanol and water at a mixed volume ratio of 15 mL: 5mL of the alumina wet sol is mixed, heated and refluxed for 3 hours at the temperature of 80 ℃ under the stirring condition, the stirring is stopped, the heating is continued for 1 hour, the mixture is cooled to the room temperature, hydrochloric acid is added to adjust the pH value to be 3, and the mixture is stirred for 10min to obtain the alumina wet sol;
(2) adding 2.55g of TEOS into a mixed solution of ethanol and water, wherein the mixing molar ratio of the ethanol to the water is 7: 3, mixing and stirring for 0.5h (no silica sol is formed in a short treatment time), and then adjusting the pH value to 2 by using hydrochloric acid to obtain a silica sol precursor solution;
(3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), stirring for 2 hours, adding ammonia water to adjust the pH value to be neutral, standing for 12 hours to form a silicon-aluminum mixed wet gel, exchanging an ethanol solvent with n-hexane without heating and aging, performing solvent exchange with n-hexane (changing the structure of the material by changing the polarity of the solution), and drying in a vacuum drying oven at 50 ℃ for 6 hours to obtain the silicon-aluminum based aerogel (the molar ratio of silicon to aluminum in the silicon-aluminum based aerogel is 1: 1); and grinding the dried silicon-aluminum-based aerogel into fine particles by using a mortar, and screening materials with the size of 40-60 meshes by using a medicine screen to perform an adsorption experiment.
0.6g of silica-alumina aerogel is weighed, and 0.06g of PbCl is weighed2Adding into a secondary reaction furnace for PbCl2And (4) performing gas adsorption experiments. Adsorbing at 800 deg.C for 40min with PbCl2The adsorption removal rate of (2) is 44.37%, which shows that the silicon-aluminum ratio in the silicon-aluminum based aerogel is reduced, so that the adsorption efficiency is greatly reduced. This is because heavy metals are solidified as silicates by the silica-alumina-based aerogel at high temperatures, and lowering the silica-alumina ratio reduces the formation of silicates and lowers the adsorption efficiency.
Example 6
The preparation method of the silicon-aluminum based aerogel comprises the following steps:
(1) 2.5g of Aluminum Isopropoxide (AIP) was added to a mixed solution of ethanol and water in a mixed volume ratio of 15 mL: 5mL of the alumina wet sol is mixed, heated and refluxed for 3 hours at the temperature of 80 ℃ under the stirring condition, the stirring is stopped, the heating is continued for 1 hour, the mixture is cooled to the room temperature, hydrochloric acid is added to adjust the pH value to be 3, and the mixture is stirred for 10min to obtain the alumina wet sol;
(2) adding 2.55g of TEOS into a mixed solution of ethanol and water, wherein the mixing molar ratio of the ethanol to the water is 7: 3, mixing and stirring for 0.5h (no silica sol is formed in a short treatment time), and then adjusting the pH value to 2 by using hydrochloric acid to obtain a silica sol precursor solution;
(3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), stirring for 2 hours, adding ammonia water to adjust the pH value to be neutral, standing for 12 hours to form a silicon-aluminum mixed wet gel, exchanging an ethanol solvent with n-hexane without heating and aging, performing solvent exchange with n-hexane (changing the structure of the material by changing the polarity of the solution), and drying in a vacuum drying oven at 50 ℃ for 6 hours to obtain the silicon-aluminum based aerogel (the molar ratio of silicon to aluminum in the silicon-aluminum based aerogel is 1: 1); and grinding the dried silicon-aluminum-based aerogel into fine particles by using a mortar, and screening materials with the size of 40-60 meshes by using a medicine screen to perform an adsorption experiment.
0.6g of silica-alumina aerogel is weighed, and 0.06g of PbCl is weighed2Adding into a secondary reaction furnace for PbCl2And (4) performing gas adsorption experiments. Adsorbing at 600 deg.C for 40min with PbCl2The adsorption removal rate of (2) is 54.25%, which shows that the adsorption temperature has great influence on the adsorption efficiency of the adsorbent, and because the temperature is reduced, the effective collision between heavy metal and the silicon-aluminum based aerogel is reduced, so that PbCl2 captured by adsorption sites is reduced, and meanwhile, the generation of silicate is not facilitated, and the adsorption efficiency is reduced.
The calculation process of the adsorption efficiency of the silicon-aluminum-based aerogel prepared in the embodiment 1-6 is as follows:
1. the mass ratio of the added heavy metal to the adsorbent is as follows:
m1for adding the mass of heavy metal, m2Is the mass of the adsorbent aerogel.
2. Determination of heavy metal content in adsorbed adsorption material
Digesting the adsorption material, and measuring the concentration w of heavy metal in the adsorbed material by utilizing ICP-MS (inductively coupled plasma-mass spectrometry)
3. Calculation of adsorption efficiency μ
V is the constant volume, C is the metal concentration measured by ICP-MS, M1Is PbCl2Molar mass of (a), m1' is the mass of the adsorbed aerogel, M, weighed by digestion2Is the molar mass of Pb, m2' is the mass of aerogel weighed after adsorption, m3Is the mass of heavy metal adsorbed by the aerogel.
TABLE 1 shows the adsorption of PbCl onto silica aerogel at 800 ℃ and the silica-alumina-based aerogel obtained in example 12Comparison of specific surface area and porosity before and after
As can be seen from table 1, the silica-alumina-based aerogel prepared in example 1 of the present invention has higher thermal stability and larger specific surface area and porosity than the silica aerogel. After high-temperature adsorption at 800 ℃, the specific surface areas of the silica aerogel and the silicon-aluminum-based aerogel prepared in example 1 are respectively reduced by 150.71m2·g-1And 71.27m2·g-1The results show that the silicon-aluminum based aerogel prepared in example 1 has a pore channel which is not easy to collapse at high temperature, has a stable structure and high thermal stability, and can be applied to adsorption of heavy metal gas in an actual pyrolysis process.
Claims (7)
1. The preparation method of the silicon-aluminum based aerogel is characterized by comprising the following steps:
(1) adding aluminum isopropoxide into a mixed solution of ethanol and water to obtain a mixed material, heating and refluxing the mixed material under a stirring condition, continuing to heat after stirring is stopped, cooling to room temperature after heating, and adjusting the pH value of the solution to be acidic to obtain alumina wet sol;
(2) adding tetraethoxysilane into a mixed solution of ethanol and water, stirring for no more than 0.5h, and adjusting the pH value of the solution to be acidic to obtain a silica sol precursor solution;
(3) and (3) mixing the alumina wet sol obtained in the step (1) with the silica sol precursor solution obtained in the step (2), adjusting the pH value of the mixed solution to be neutral after stirring, standing the mixed solution for at least 12 hours to form silicon-aluminum mixed wet gel, performing solvent exchange by using n-hexane, and drying the silicon-aluminum mixed wet gel in a vacuum drying oven to obtain the silicon-aluminum-based aerogel.
2. The method for preparing a silicoalumino-aerogel according to claim 1, characterized in that: in the step (1), the mixing volume ratio of the ethanol to the water is 15-30: 5-10.
3. The method for preparing a silicoalumino-aerogel according to claim 1, characterized in that: in the step (2), the mixing molar ratio of the ethanol to the water is 5-7: 1-3.
4. The method for preparing a silicoalumino-aerogel according to claim 1, characterized in that: in the step (3), the drying temperature is 50-60 ℃, and the drying time is 6-10 h.
5. The method for preparing a silicoalumino-aerogel according to claim 1, characterized in that: in the step (3), the molar ratio of silicon-aluminum elements in the obtained silicon-aluminum based aerogel is 1: 1.
6. The use of the silica-alumina based aerogel obtained by the method for preparing a silica-alumina based aerogel according to claim 1 for the adsorption of heavy metal gases.
7. The application of the silicon-aluminum based aerogel prepared by the preparation method of the silicon-aluminum based aerogel according to claim 6 in the aspect of adsorbing heavy metal gas is characterized in that: the silicon-aluminum-based aerogel is used for adsorbing heavy metal gas in the pyrolysis process, and the temperature in the pyrolysis process is 600-900 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011492751.1A CN112624166B (en) | 2020-12-16 | 2020-12-16 | Preparation method of silicon-aluminum-based aerogel and application of prepared silicon-aluminum-based aerogel in heavy metal gas adsorption |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011492751.1A CN112624166B (en) | 2020-12-16 | 2020-12-16 | Preparation method of silicon-aluminum-based aerogel and application of prepared silicon-aluminum-based aerogel in heavy metal gas adsorption |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN112624166A true CN112624166A (en) | 2021-04-09 |
| CN112624166B CN112624166B (en) | 2023-11-17 |
Family
ID=75316247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011492751.1A Active CN112624166B (en) | 2020-12-16 | 2020-12-16 | Preparation method of silicon-aluminum-based aerogel and application of prepared silicon-aluminum-based aerogel in heavy metal gas adsorption |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112624166B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113797880A (en) * | 2021-08-24 | 2021-12-17 | 天津朗华科技发展有限公司 | Oil stain wastewater adsorbent and preparation method and application thereof |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20150104357A1 (en) * | 2013-10-15 | 2015-04-16 | Chung Yuan Christian University | Porous Silica Aerogel Composite Membrane And Method For Making The Same And Carbon Dioxide Sorption Device |
| TW201632353A (en) * | 2015-03-03 | 2016-09-16 | 國立臺灣大學 | Vacuum membrane distillation device and method including hydrophobic porous silica aerogel composite membrane |
| CN108607526A (en) * | 2018-05-15 | 2018-10-02 | 芜湖市宝艺游乐科技设备有限公司 | It is a kind of to utilize coal ash for manufacturing for SiO2The method of the cuprous adsorbent of gel combined oxidation |
| CN109621849A (en) * | 2019-01-25 | 2019-04-16 | 浙江工业大学 | A kind of atmospheric preparation method of coated with silica alumina composite aeroge |
| CN110038493A (en) * | 2019-04-30 | 2019-07-23 | 齐鲁工业大学 | A kind of atmospheric preparation method of Al2O3-SiO2 composite aerogel |
| CN111659324A (en) * | 2020-04-28 | 2020-09-15 | 南京工业大学 | Ozone catalytic system composite aerogel and preparation method and application thereof |
| CN111773928A (en) * | 2020-07-02 | 2020-10-16 | 中国科学院城市环境研究所 | Aerogel composite membrane and preparation method and application thereof |
-
2020
- 2020-12-16 CN CN202011492751.1A patent/CN112624166B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20150104357A1 (en) * | 2013-10-15 | 2015-04-16 | Chung Yuan Christian University | Porous Silica Aerogel Composite Membrane And Method For Making The Same And Carbon Dioxide Sorption Device |
| TW201632353A (en) * | 2015-03-03 | 2016-09-16 | 國立臺灣大學 | Vacuum membrane distillation device and method including hydrophobic porous silica aerogel composite membrane |
| CN108607526A (en) * | 2018-05-15 | 2018-10-02 | 芜湖市宝艺游乐科技设备有限公司 | It is a kind of to utilize coal ash for manufacturing for SiO2The method of the cuprous adsorbent of gel combined oxidation |
| CN109621849A (en) * | 2019-01-25 | 2019-04-16 | 浙江工业大学 | A kind of atmospheric preparation method of coated with silica alumina composite aeroge |
| CN110038493A (en) * | 2019-04-30 | 2019-07-23 | 齐鲁工业大学 | A kind of atmospheric preparation method of Al2O3-SiO2 composite aerogel |
| CN111659324A (en) * | 2020-04-28 | 2020-09-15 | 南京工业大学 | Ozone catalytic system composite aerogel and preparation method and application thereof |
| CN111773928A (en) * | 2020-07-02 | 2020-10-16 | 中国科学院城市环境研究所 | Aerogel composite membrane and preparation method and application thereof |
Non-Patent Citations (1)
| Title |
|---|
| HUIJUN YU ET AL.: "Quartz fiber reinforced Al2O3-SiO2 aerogel composite with highly thermal stability by ambient pressure drying" * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113797880A (en) * | 2021-08-24 | 2021-12-17 | 天津朗华科技发展有限公司 | Oil stain wastewater adsorbent and preparation method and application thereof |
| CN113797880B (en) * | 2021-08-24 | 2023-11-24 | 天津朗华科技发展有限公司 | Greasy dirt wastewater adsorbent and preparation method and application thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN112624166B (en) | 2023-11-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Cividanes et al. | Review of mullite synthesis routes by sol–gel method | |
| CN108889329B (en) | Carbon nitride quantum dot modified hierarchical pore TiO2-SiO2Photocatalyst and process for producing the same | |
| Zawrah et al. | Facile and economic synthesis of silica nanoparticles | |
| KR20120070948A (en) | Manufacturing method of hydropobic silica aerogel powder with insulating performance | |
| CN104826582A (en) | Preparation method of graphene-mesoporous silica aerogel | |
| KR102092769B1 (en) | Method of preparing for silica aerogel and silica aerogel prepared by the same | |
| TW201132589A (en) | Synthetic amorphous silica powder and process for producing the same | |
| JP2019531443A (en) | Method for producing hydrophobic heat insulating material | |
| KR102092770B1 (en) | Method of preparing for silica aerogel and silica aerogel prepared by the same | |
| KR20180126874A (en) | Method preparing silicon carbide particle and the silicon carbide particle prepared the same | |
| CN112624166A (en) | Preparation method of silicon-aluminum-based aerogel and application of prepared silicon-aluminum-based aerogel in aspect of adsorbing heavy metal gas | |
| TWI589351B (en) | Carbon adsorbent, the manufacturing method thereof, and the using method thereof | |
| Mu et al. | CO2 high-temperature sorbent (Al, Fe, Ti) CO-doped Li4SiO4 from fly ash-derived SiO2 aerogel: In-situ synthesis, enhanced capture ability and long cycle stability | |
| JP3005678B2 (en) | Method for producing mesoporous silica material | |
| Yang et al. | Facile and surfactant‐free route to nanocrystalline mesoporous tin oxide | |
| JP4488191B2 (en) | Method for producing spherical silica-based mesoporous material | |
| CN111362672A (en) | Preparation process of bauxite-based ceramic filler | |
| JP2009190909A (en) | Method for surface-treating of mesoporous silica, and method for producing slurry composition for adding to resin, filler for resin and resin composition | |
| KR102517174B1 (en) | Preparation method of silicon carbides particles | |
| CN107128925A (en) | A kind of method that non-hydrolytic sol-gel combination carbothermic method prepares SiC powder | |
| CN111362274B (en) | Micron-sized spherical lithium-based CO2Adsorbent and preparation method thereof | |
| CN114408934A (en) | Preparation method of nano silicon dioxide | |
| Cai et al. | Efficient carbon dioxide adsorption properties of cellular structure Li4SiO4 sorbents prepared by additive manufacturing based on polymer-derived ceramics strategy | |
| CN106006659A (en) | Preparation method of titanium-aluminum molecular sieve photocatalyst | |
| KR101014595B1 (en) | Method for fabricating tin dioxide nano sol and porous composite using the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |