CN113134347A - Preparation method and application of heteroatom porous carbon - Google Patents
Preparation method and application of heteroatom porous carbon Download PDFInfo
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- CN113134347A CN113134347A CN202110310223.8A CN202110310223A CN113134347A CN 113134347 A CN113134347 A CN 113134347A CN 202110310223 A CN202110310223 A CN 202110310223A CN 113134347 A CN113134347 A CN 113134347A
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 50
- 125000005842 heteroatom Chemical group 0.000 title claims abstract description 48
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- 241000931705 Cicada Species 0.000 claims abstract description 38
- 238000001035 drying Methods 0.000 claims abstract description 38
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 19
- 239000000843 powder Substances 0.000 claims abstract description 19
- 239000007864 aqueous solution Substances 0.000 claims abstract description 18
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims abstract description 17
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims abstract description 17
- 238000009210 therapy by ultrasound Methods 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- 239000000725 suspension Substances 0.000 claims abstract description 14
- -1 polytetrafluoroethylene Polymers 0.000 claims abstract description 13
- 238000007873 sieving Methods 0.000 claims abstract description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000005406 washing Methods 0.000 claims abstract description 8
- 238000001816 cooling Methods 0.000 claims abstract description 7
- 239000008367 deionised water Substances 0.000 claims abstract description 7
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 7
- 238000001914 filtration Methods 0.000 claims abstract description 7
- 239000012535 impurity Substances 0.000 claims abstract description 7
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims abstract description 7
- 239000004810 polytetrafluoroethylene Substances 0.000 claims abstract description 7
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 7
- 239000010935 stainless steel Substances 0.000 claims abstract description 7
- 239000002351 wastewater Substances 0.000 claims abstract description 7
- 230000035484 reaction time Effects 0.000 claims description 6
- 238000004506 ultrasonic cleaning Methods 0.000 claims description 3
- 239000000356 contaminant Substances 0.000 claims 1
- 239000003054 catalyst Substances 0.000 abstract description 8
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000007833 carbon precursor Substances 0.000 abstract description 2
- 238000004140 cleaning Methods 0.000 abstract 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 14
- 239000000975 dye Substances 0.000 description 9
- IQFVPQOLBLOTPF-HKXUKFGYSA-L congo red Chemical compound [Na+].[Na+].C1=CC=CC2=C(N)C(/N=N/C3=CC=C(C=C3)C3=CC=C(C=C3)/N=N/C3=C(C4=CC=CC=C4C(=C3)S([O-])(=O)=O)N)=CC(S([O-])(=O)=O)=C21 IQFVPQOLBLOTPF-HKXUKFGYSA-L 0.000 description 8
- 239000003575 carbonaceous material Substances 0.000 description 6
- 239000002957 persistent organic pollutant Substances 0.000 description 5
- 239000001044 red dye Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 238000002835 absorbance Methods 0.000 description 3
- 230000002195 synergetic effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000000527 sonication Methods 0.000 description 2
- 238000012876 topography Methods 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 230000010718 Oxidation Activity Effects 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 206010043275 Teratogenicity Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 239000000979 synthetic dye Substances 0.000 description 1
- 231100000211 teratogenicity Toxicity 0.000 description 1
Images
Classifications
-
- 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
- B01J20/28054—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 surface properties or porosity
-
- 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
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/34—Organic compounds containing oxygen
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/38—Organic compounds containing nitrogen
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/40—Organic compounds containing sulfur
Abstract
The invention discloses a preparation method of heteroatom porous carbon, which specifically comprises the following steps: firstly, putting the cicada slough into absolute ethyl alcohol for ultrasonic treatment, cleaning soluble impurities, drying, crushing and sieving to obtain cicada slough powder; dispersing the cicada slough powder in a ferric chloride aqueous solution to obtain uniformly dispersed suspension, putting the suspension into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, carrying out hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain the heteroatom porous carbon. Cicada slough is used as a carbon precursor, and the iron-doped heteroatom porous carbon is prepared by a one-step method and is used as a catalyst of Fenton-like reaction. The raw material has wide source, low cost and simple preparation process, and has great application potential in treating dye wastewater.
Description
Technical Field
The invention belongs to the technical field of carbon material preparation, and particularly relates to a preparation method of heteroatom porous carbon and application of the heteroatom porous carbon.
Background
Water has long been one of the most important resources for human survival and development. With the discharge of various pollutants, water pollution is becoming more serious, so that the water pollution problem is receiving increasing attention. The synthetic dye is the main component of sewage, has strong stability, carcinogenicity and teratogenicity, and has great threat to ecological environment and human health.
Heteroatom-doped carbon is one of the most potential materials for remediation of contaminated groundwater and industrial wastewater, because the doping elements affect the surface polarity, electronic conductivity, active sites and wettability of the carbon material, thereby significantly improving removal efficiency. The introduction of hetero atoms (nitrogen, oxygen, sulfur, phosphorus) is helpful for electron transfer, and increases the surface polarity and active sites, thereby enhancing the catalytic effect. Therefore, it is of great significance to design and synthesize heteroatom-doped carbon materials for environmental applications.
The cicada slough is a semitransparent and glossy shell, takes chitin as a main component, also contains abundant nonmetal heteroatoms, and has great potential in the aspect of removing organic pollutants.
Disclosure of Invention
The invention aims to provide a preparation method of heteroatom porous carbon, which improves the adsorption and degradation capability of the porous carbon on organic dye.
The invention also aims to provide application of the heteroatom porous carbon in removal of organic pollutants in dye wastewater.
The technical scheme adopted by the invention is that the preparation method of the heteroatom porous carbon is implemented according to the following steps:
step 1, putting the cicada slough into absolute ethyl alcohol for ultrasonic treatment, and cleaning soluble impurities;
step 2, drying the cicada slough obtained in the step 1, crushing and sieving to obtain cicada slough powder;
step 3, dispersing the cicada slough powder obtained in the step 2 in a ferric chloride aqueous solution to obtain a uniformly dispersed suspension;
and 4, putting the suspension obtained in the step 3 into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, performing hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain the heteroatom porous carbon.
The present invention is also characterized in that,
in the step 1, the mass ratio of the cicada slough to the absolute ethyl alcohol is 1: 8; the ultrasonic treatment time is 30min-50 min.
In the step 2, the drying temperature is 50-70 ℃, and the drying time is 12-24 h; a50-mesh screen is adopted for sieving.
In the step 3, the mass ratio of the cicada slough powder to the ferric chloride aqueous solution is 1: 29;
the concentration of the ferric chloride aqueous solution is 0.05 mol/L.
In the step 4, the hydrothermal reaction temperature is 170-190 ℃, and the hydrothermal reaction time is 12-14 h; the drying temperature is 70-90 ℃, and the drying time is 12-14 h.
The invention adopts another technical scheme that the heteroatom porous carbon can be applied to removal of organic pollutants in dye wastewater.
The invention has the beneficial effects that:
(1) the invention relates to a preparation method of heteroatom porous carbon, which takes periostracum cicada as a carbon precursor and adopts a one-step method to prepare the iron-doped heteroatom porous carbon as a catalyst of Fenton-like reaction. The technology has the advantages of wide raw material source, low cost, simple preparation process and great application potential in treating dye wastewater;
(2) according to the preparation method of the heteroatom porous carbon, the prepared porous carbon can have good removal capability on organic pollutants through the combined action of sonochemistry and Fenton reaction, and has good application prospects in the field of water purification.
Drawings
FIG. 1 is a first scanning electron microscope topography of the iron-doped heteroatom porous carbon in the preparation method of the heteroatom porous carbon of the present invention;
FIG. 2 is a scanning electron microscope topography of the iron-doped heteroatom porous carbon in the preparation method of the heteroatom porous carbon of the invention (II);
FIG. 3 is an absorbance curve before and after adsorption of the iron-doped heteroatom porous carbon to Congo red dye in the preparation method of the heteroatom porous carbon of the present invention.
Detailed Description
The present invention will be described in detail below with reference to the accompanying drawings and specific embodiments.
The invention relates to a preparation method of heteroatom porous carbon, which is implemented according to the following steps:
step 1, putting the cicada slough into absolute ethyl alcohol for ultrasonic treatment, and cleaning soluble impurities;
the mass ratio of the cicada slough to the absolute ethyl alcohol is 1: 8;
the ultrasonic treatment time is 30min-50 min;
step 2, drying the cicada slough obtained in the step 1, crushing and sieving to obtain cicada slough powder;
the drying temperature is 50-70 ℃, and the drying time is 12-24 h; a screen mesh of 50 meshes is adopted during sieving;
step 3, dispersing the cicada slough powder obtained in the step 2 in a ferric chloride aqueous solution to obtain a uniformly dispersed suspension;
the mass ratio of the cicada slough powder to the ferric chloride aqueous solution is 1: 29;
the concentration of the ferric chloride aqueous solution is 0.05 mol/L;
step 4, putting the suspension obtained in the step 3 into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, performing hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain heteroatom porous carbon;
the hydrothermal reaction temperature is 170-190 ℃, and the hydrothermal reaction time is 12-14 h;
the drying temperature is 70-90 ℃, and the drying time is 12-14 h;
the heteroatom porous carbon prepared by the method can be applied to removal of organic pollutants in dye wastewater, and the specific method comprises the following steps: and mixing the heteroatom porous carbon with hydrogen peroxide, carrying out ultrasonic treatment for 30-60 min, and degrading Congo red dye in the wastewater by using Fenton reaction and ultrasonic treatment.
Example 1
The invention relates to a preparation method of heteroatom porous carbon, which is implemented according to the following steps:
step 1, 50g of cicada slough is placed into 500mL of absolute ethyl alcohol for ultrasonic treatment, and soluble impurities are washed away;
the ultrasonic treatment time is 30 min;
step 2, drying the cicada slough obtained in the step 1, crushing and sieving to obtain cicada slough powder;
the drying temperature is 50 ℃, and the drying time is 12 h; a screen mesh of 50 meshes is adopted during sieving;
step 3, dispersing 5g of the cicada slough powder obtained in the step 2 in 50mL of iron chloride aqueous solution to obtain uniformly dispersed suspension;
the concentration of the ferric chloride aqueous solution is 0.05 mol/L;
step 4, putting the suspension obtained in the step 3 into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, performing hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain heteroatom porous carbon;
the hydrothermal reaction temperature is 170 ℃, and the hydrothermal reaction time is 12 h;
the drying temperature is 70 ℃, and the drying time is 12 hours;
when hydrogen peroxide was added to the iron-doped heteroatom porous carbon prepared in example 1, the sample had a congo red removal rate of 94.24% without sonication, whereas the sample had a congo red removal rate of 99.45% under sonication. The increase of the dye removal rate is due to the synergistic effect of sonochemistry and Fenton reaction, and the adsorption capacity of the carbon material is enhanced.
Example 2
The invention relates to a preparation method of heteroatom porous carbon, which is implemented according to the following steps:
step 1, 50g of cicada slough is placed into 500ml of absolute ethyl alcohol for ultrasonic treatment, and soluble impurities are washed away;
the ultrasonic treatment time is 40 min;
step 2, drying the cicada slough obtained in the step 1, crushing and sieving to obtain cicada slough powder;
the drying temperature is 60 ℃, and the drying time is 13 h; a screen mesh of 50 meshes is adopted during sieving;
step 3, dispersing the cicada slough powder obtained in the step 2 in a ferric chloride aqueous solution to obtain a uniformly dispersed suspension;
the mass ratio of the cicada slough powder to the ferric chloride aqueous solution is 1: 29; the concentration of the ferric chloride aqueous solution is 0.05 mol/L;
step 4, putting the suspension obtained in the step 3 into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, performing hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain heteroatom porous carbon;
the hydrothermal reaction temperature is 180 ℃, and the hydrothermal reaction time is 13 h;
the drying temperature is 80 ℃, and the drying time is 13 h;
example 3
The invention relates to a preparation method of heteroatom porous carbon, which is implemented according to the following steps:
step 1, putting 5g of cicada slough into 500ml of absolute ethyl alcohol for ultrasonic treatment, and washing off soluble impurities;
the ultrasonic treatment time is 50 min;
step 2, drying the cicada slough obtained in the step 1, crushing and sieving to obtain cicada slough powder;
the drying temperature is 70 ℃, and the drying time is 14 h; a screen mesh of 50 meshes is adopted during sieving;
step 3, dispersing the cicada slough powder obtained in the step 2 in a ferric chloride aqueous solution to obtain a uniformly dispersed suspension;
the mass ratio of the cicada slough powder to the ferric chloride aqueous solution is 1: 29; the concentration of the ferric chloride aqueous solution is 0.05 mol/L;
step 4, putting the suspension obtained in the step 3 into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, performing hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain heteroatom porous carbon;
the hydrothermal reaction temperature is 190 ℃, and the hydrothermal reaction time is 14 h;
the drying temperature is 90 ℃, and the drying time is 14 h;
fig. 1 and 2 are scanning electron microscope pictures of the fe-doped heteroatom carbon prepared in example 1, wherein the heteroatom carbon still has a porous structure after being doped with fe element surface elements, and the surface of the heteroatom carbon is covered with some fine particles. In addition, as shown in fig. 2, the iron-doped heteroatom carbon has a three-dimensional network structure.
Fig. 3 is an absorbance curve before and after the heteroatom porous carbon prepared in example 1 adsorbs congo red dye, and it can be seen that the absorbance curves of the heteroatom porous carbon adsorbed congo red dye are almost the same regardless of whether hydrogen peroxide is added. Indicating that hydrogen peroxide has little effect on dye removal in the absence of iron ions. After the iron ions are added, most of dye can be removed through the synergistic effect of the iron ions and the hydrogen peroxide, and the removal rate of the Congo red by the porous carbon material is greatly improved through ultrasonic treatment.
According to the preparation method of the heteroatom porous carbon, the adsorption mechanism of the porous carbon on Congo red dye is that organic matters and hydrogen peroxide are diffused to active sites on the surface of a catalyst and are adsorbed, then under the catalytic action of the catalyst, iron ions and the hydrogen peroxide are reacted in series to generate hydroxyl radicals, and the hydroxyl radicals have high oxidation activity, so that a radical chain reaction is initiated, the organic matters are oxidized and degraded, and finally, degradation products are desorbed from the surface of the catalyst and are diffused in a main body of a solution, so that the efficient and rapid degradation of the organic matters is realized.
The preparation method takes the cicada slough as a precursor, and adopts a one-step method to prepare a novel heteroatom porous carbon material as a Fenton-like reagent catalyst. Then the catalyst is enhanced in catalysis and stability through the synergistic effect of sonochemistry and Fenton reaction, and the performance of the catalyst in the aspect of removing industrial pollution is improved. The technology has the advantages of wide raw material source, low cost, simple preparation process and great application potential in the aspect of dye removal.
Claims (6)
1. The preparation method of the heteroatom porous carbon is characterized by comprising the following steps:
step 1, putting the cicada slough into absolute ethyl alcohol for ultrasonic treatment, and cleaning soluble impurities;
step 2, drying the cicada slough obtained in the step 1, crushing and sieving to obtain cicada slough powder;
step 3, dispersing the cicada slough powder obtained in the step 2 in a ferric chloride aqueous solution to obtain a uniformly dispersed suspension;
and 4, putting the suspension obtained in the step 3 into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, performing hydrothermal reaction, naturally cooling, filtering, washing with deionized water for several times, and drying to obtain the heteroatom porous carbon.
2. The method for preparing heteroatom porous carbon according to claim 1, wherein in the step 1, the mass ratio of periostracum cicada to absolute ethyl alcohol is 1: 8; the ultrasonic treatment time is 30min-50 min.
3. The method for preparing the heteroatom porous carbon according to claim 1, wherein in the step 2, the drying temperature is 50-70 ℃, and the drying time is 12-24 h; a50-mesh screen is adopted for sieving.
4. The method for preparing heteroatom porous carbon as claimed in claim 1, wherein in the step 3, the mass ratio of the periostracum cicadae powder to the ferric chloride aqueous solution is 1: 29; the concentration of the ferric chloride aqueous solution is 0.05 mol/L.
5. The method for preparing the heteroatom porous carbon according to claim 1, wherein in the step 4, the hydrothermal reaction temperature is 170-190 ℃, and the hydrothermal reaction time is 12-14 h; the drying temperature is 70-90 ℃, and the drying time is 12-14 h.
6. A method of preparing the heteroatomic porous carbon according to any one of claims 1-5 that can be used in the removal of organic contaminants from dye wastewater.
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CN113845115A (en) * | 2021-10-12 | 2021-12-28 | 西安理工大学 | Preparation method and application of heteroatom self-doped biomass porous carbon |
CN113845115B (en) * | 2021-10-12 | 2024-04-05 | 西安理工大学 | Preparation method and application of heteroatom self-doped biomass porous carbon |
CN114958365A (en) * | 2022-06-30 | 2022-08-30 | 北京兴德通医药科技股份有限公司 | Preparation method and application of periostracum cicadae carbon quantum dots |
CN114958365B (en) * | 2022-06-30 | 2023-08-08 | 北京兴德通医药科技股份有限公司 | Preparation method and application of cicada slough carbon quantum dots |
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