CN113753892B - Biomass-based activated carbon material - Google Patents
Biomass-based activated carbon material Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/318—Preparation characterised by the starting materials
- C01B32/324—Preparation characterised by the starting materials from waste materials, e.g. tyres or spent sulfite pulp liquor
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- 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
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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
- B01J20/20—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
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/342—Preparation characterised by non-gaseous activating agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/485—Plants or land vegetals, e.g. cereals, wheat, corn, rice, sphagnum, peat moss
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- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
Abstract
A biomass-based activated carbon material comprises the following raw materials in parts by weight: 1 part of peony seed meal; 1-2 parts of fir bark. The method for preparing the biomass-based activated carbon material by using the peony seed meal rich in peony seed oil as the raw material can improve the utilization value of the peony seed meal. The method can better solve the problem of difficult treatment of the desulfurization waste liquid by using the desulfurization waste liquid as the activating agent, and can reduce the using amount of the industrial activating agent and the preparation cost of the activated carbon material. The method uses the peony seed meal as a raw material, can fully utilize residual peony seed oil in the peony seed meal, carries out in-situ nitrogen element doping on the obtained biomass-based active carbon material in the carbonization and activation process, adjusts the surface performance of the material, improves the surface pH value of the active carbon material, and adsorbs CO for the active carbon 2 Providing a large number of active sites. The method for preparing the biomass-based activated carbon material by using the desulfurization waste liquid and the amino sodium through two-step activation can reduce the activation temperature to 450-550 ℃, thereby reducing the energy consumption for preparing the activated carbon.
Description
Technical Field
The invention belongs to the field of preparation of activated carbon materials, and particularly relates to a biomass-based activated carbon material.
Background
With the continuous development of society, the increasingly serious greenhouse effect causes climate abnormity, and the wide attention of the world is attracted; CO discharged by coal-fired power plant flue gas 2 Is an important reason for the growing serious greenhouse effect. Therefore, how to effectively capture CO from flue gas 2 Reduction of artificial CO 2 The emission has important significance for relieving global climate change. The activated carbon has specific surfaceThe method has the advantages of large volume, adjustable aperture, good surface hydrophobicity, low price, easy obtainment and the like, and is widely applied to the separation of gases such as flue gas, carbon dioxide and the like. At present, however, in order to improve the pore structure and CO of activated carbon 2 Adsorption performance, use of large amount of KOH or K in the preparation process of activated carbon 2 CO 3 And the like. The great use of the activating agent for a long time not only causes equipment corrosion and serious environmental pollution, but also increases the preparation cost of the activated carbon. Meanwhile, the research of the literature finds that the N atoms have structural characteristics similar to those of the carbon atoms, and when the N atoms are doped to replace some carbon atoms in the carbon material, the pore structure performance of the activated carbon adsorbent can be adjusted, and the surface performance of the material can also be adjusted, so that the pH value of the surface of the activated carbon material is improved, and CO is adsorbed by the activated carbon adsorbent 2 Providing a large number of active sites.
In addition, the desulfurization waste liquid generated in the desulfurization process of the coke oven gas is a mixed pollutant containing various toxic substances, mainly contains components such as ammonium thiosulfate, ammonium thiocyanate, ammonium sulfate, ammonium sulfite, hydroquinone, suspended sulfur and the like, cannot be directly treated by a biochemical method, and cannot be directly discharged. Therefore, how to effectively treat the coking desulfurization waste liquid is a difficult problem to be solved urgently in coking enterprises.
Sher et al prepared carbon dioxide adsorbents using walnut shells as a carbon source and KOH as an activator, but the mass ratio of KOH to walnut shells reached 4 (Sher et al, development of biological derived high viscosity soil adsorbents for postcom CO2 capture, fuel 282 (2020) 118506-118518). Cai et al purify styrene and divinylbenzene to prepare a carbon precursor, and then use KOH as an activator to prepare a spherical carbon material for carbon dioxide adsorption, not only the synthesis process is complicated, but also the mass ratio of KOH to the carbon source reaches 4 (Cai et al metal-free core-shell structured N-bonded carbon/carbon heterojunction for carbon dioxide adsorption CO) 2 capture, carbon150 (2019) 43-51). Therefore, the development of an activated carbon material which can be simply prepared and has high adsorption capacity and low cost is very important for capturing carbon dioxide.
Disclosure of Invention
The invention provides a biomass-based activated carbon material, which is used for overcoming the defects in the prior art.
The invention is realized by the following technical scheme:
a biomass-based active carbon material comprises the following raw materials in parts by weight: 1 part of peony seed meal; 1-2 parts of fir bark.
The preparation method of the biomass-based activated carbon material comprises the following steps:
the method comprises the following steps: drying the peony seed meal and the fir bark at 120 ℃, respectively, crushing to 300-500 meshes, and then mixing to obtain a mixed raw material A;
step two: mixing the mixed raw material A and the desulfurization waste liquid according to the solid-liquid ratio of 1g/5-20ml, performing ultrasonic impregnation for 2-6h under the condition of the ultrasonic frequency of 25-40KHz, drying at 100-150 ℃, and performing carbonization and activation for 2-4h under the conditions of the temperature of 500-700 ℃ and the temperature rise rate of carbonization and activation of 5-8 ℃/min, wherein the carbonization and activation are performed under the condition of air isolation; obtaining a mixed carbon material B;
step three: and mixing the obtained mixed carbon material B and sodium amide according to the mass ratio of 1-2, and then activating for 1.5-3h in an air-isolated manner under the conditions that the temperature is 450-550 ℃ and the activation heating rate is 5-8 ℃/min, so as to obtain the biomass-based active carbon material.
The biomass-based activated carbon material has the specific surface area of 1033-2951cm 2 /g。
The total pore volume of the biomass-based activated carbon material is 0.57-1.60cm 3 /g。
The total volume of the micropores of the biomass-based activated carbon material is 0.52-1.25cm 3 /g。
The biomass-based activated carbon material has the adsorption temperature of 0-50 ℃ and the adsorption pressure of 0.01-0.1MPa.
The biomass-based activated carbon material is applied to adsorbing and capturing carbon dioxide.
The invention has the advantages that: the invention prepares biomass-based activated carbon by taking peony seed meal rich in peony seed oil as a raw materialThe material can improve the utilization value of peony seed meal, and the fir bark is used as the raw material to improve the pore structure performance of the activated carbon material. The method can better solve the problem of difficult treatment of the desulfurization waste liquid by using the desulfurization waste liquid as the activating agent, and can reduce the using amount of the industrial activating agent and the preparation cost of the activated carbon material. The method uses the peony seed meal as a raw material, can fully utilize residual peony seed oil in the peony seed meal, carries out in-situ nitrogen element doping on the obtained biomass-based active carbon material in the carbonization and activation process, adjusts the surface performance of the material, improves the surface pH value of the active carbon material, and adsorbs CO for the active carbon 2 Providing a large number of active sites. The method for preparing the biomass-based activated carbon material by using the desulfurization waste liquid and the amino sodium through two-step activation can reduce the activation temperature to 450-550 ℃, thereby reducing the energy consumption for preparing the activated carbon.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the description of the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and those skilled in the art can obtain other drawings based on the drawings without inventive labor.
FIG. 1 is a diagram of a peony seed meal of the present invention;
FIG. 2 is a graph of the pore size distribution of biomass-based activated carbon material prepared by the present invention;
FIG. 3 shows CO of biomass-based activated carbon material prepared by the present invention 2 Adsorption capacity graph.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1:
(1) Preparing a biomass-based activated carbon material:
drying 25g of peony seed meal and 25g of fir bark at 120 ℃, then respectively crushing to 300 meshes, and then mixing the crushed peony seed meal and the fir bark raw material to obtain a mixed raw material A; ultrasonically dipping the mixed raw material A in 500ml of desulfurization waste liquid for 2 hours at the ultrasonic frequency of 25KHz, and then drying at the temperature of 100 ℃; then carbonizing and activating for 2 hours at the temperature of 600 ℃ under the nitrogen condition, wherein the carbonization and activation temperature rate is 5 ℃/min, and obtaining a mixed carbon material B; then, physically mixing the obtained mixed carbon material B and sodium amide according to the mass ratio of 1;
(2) Testing the performance of the biomass-based active carbon material:
CO of a sample at 25 ℃ was measured using a 3H-2000PS2 type specific surface and pore size analyzer manufactured by Beijing Behcard instruments science and technology Ltd 2 Adsorption isotherm. 0.15g of biomass-based activated carbon was packed in the test tube, and the activated carbon was heated to 200 ℃ and maintained for 4 hours to remove impurity gases in the sample. Then reducing the temperature to 25 ℃ at 99.99% 2 Adsorption is carried out in the atmosphere. The carbon dioxide adsorption amount of the biomass-based activated carbon under these conditions was 3.3mmol/g, and the carbon dioxide adsorption amount curve thereof is shown in FIG. 3.
Subjecting biomass-based activated carbon material to 10 carbon dioxide adsorption and analysis tests using the 3H-2000PS2 type specific surface and pore size analyzer described above, the adsorption process being 99.99% CO at 25 deg.C 2 The analysis is carried out under the atmosphere and the analysis is carried out at 200 ℃. 0.15g of adsorbent was packed in the test tube and the temperature was raised to 200 ℃ for 4 hours. The temperature was then reduced to 25 ℃ and adsorption was carried out under a carbon dioxide atmosphere. After the adsorption process is finished, the temperature is increased to 200 ℃, and the biomass-based activated carbon is desorbed for 4 hours at 200 ℃. Then the temperature is reduced to 25 ℃, and the reaction is carried out again in the atmosphere of carbon dioxideAdsorption reaction is carried out, and the process is repeated for 10 times. Under the condition, after 10 times of adsorption/desorption circulation processes, the adsorption capacity of the biomass-based composite activated carbon can still reach 3.296mmol/g, and the adsorption capacity is only reduced by 0.12%. The biomass-based composite activated carbon has better carbon dioxide adsorption cycle stability.
Example 2:
(1) Preparing a biomass-based activated carbon material:
drying 20g of peony seed meal and 30g of fir bark at 120 ℃, then respectively crushing to 400 meshes, and then mixing the crushed peony seed meal and the fir bark raw material to obtain a mixed raw material A; ultrasonically dipping the mixed raw material A in 500ml of desulfurization waste liquid for 2 hours at the ultrasonic frequency of 25KHz, and then drying at the temperature of 100 ℃; then carbonizing and activating for 2 hours at the temperature of 600 ℃ under the nitrogen condition, wherein the temperature rate of carbonization and activation is 5 ℃/min, and obtaining a mixed carbon material B; then, physically mixing the obtained mixed carbon material B and sodium amide according to the mass ratio of 1;
(2) Testing the performance of the biomass-based active carbon material:
CO of a sample at 25 ℃ was measured using a 3H-2000PS2 type specific surface and pore size analyzer manufactured by Beijing Behcard instruments science and technology Ltd 2 Adsorption isotherms. 0.15g of biomass-based composite activated carbon was packed in a test tube, and the activated carbon was heated to 200 ℃ and maintained for 4 hours to remove impurity gases in the sample. The temperature was then reduced to 25 ℃ and adsorption was carried out under carbon dioxide atmosphere. Under the condition, the carbon dioxide adsorption capacity of the biomass-based composite activated carbon is 3.24mmol/g.
The biomass-based composite activated carbon material was subjected to carbon dioxide adsorption analysis test 10 times using the 3H-2000PS2 type specific surface and pore size analyzer described above, wherein the adsorption process was such that the content of CO was 99.99% at 25 deg.C 2 The analysis is carried out under the atmosphere and at 200 ℃. 0.15g of adsorbent was packed in the test tube and the temperature was raised to 200 ℃ for 4 hours. Then the temperature is reduced to 25 ℃, and the reaction is carried out under the atmosphere of carbon dioxideAnd (5) adsorbing. After the adsorption process was completed, the temperature was again raised to 200 ℃ and the adsorbent was allowed to desorb at 200 ℃ for 4 hours. Then, the temperature is reduced to 25 ℃, the adsorption reaction is carried out again under the carbon dioxide atmosphere, and the process is repeated for 10 times. Under the condition, after 10 times of adsorption/desorption circulation processes, the adsorption capacity of the biomass-based composite activated carbon can still reach 3.237mmol/g, and the adsorption capacity is only reduced by 0.1%. The biomass-based activated carbon has better carbon dioxide adsorption cycle stability.
Example 3:
preparing a biomass-based activated carbon material:
drying 15g of peony seed meal and 30g of fir bark at 120 ℃, then respectively crushing to 400 meshes, and then mixing the crushed peony seed meal and the fir bark raw material to obtain a mixed raw material A; ultrasonically dipping the mixed raw material A in 450ml of desulfurization waste liquid for 2 hours at the ultrasonic frequency of 25KHz, and then drying at the temperature of 120 ℃; then carbonizing and activating for 2 hours at the temperature of 600 ℃ under the nitrogen condition, wherein the temperature rate of carbonization and activation is 5 ℃/min, and obtaining a mixed carbon material B; then, physically mixing the obtained mixed carbon material B and sodium amide according to the mass ratio of 1;
(2) Testing the performance of the biomass-based active carbon material:
CO of a sample at 25 ℃ was measured using a 3H-2000PS2 type specific surface and pore size analyzer manufactured by Beijing Behcard instruments science and technology Ltd 2 Adsorption isotherms. 0.15g of biomass-based activated carbon was packed in the test tube, and the activated carbon was heated to 200 ℃ and maintained for 4 hours to remove impurity gases in the sample. The temperature was then reduced to 25 ℃ and adsorption was carried out under a carbon dioxide atmosphere. Under the condition, the carbon dioxide adsorption capacity of the biomass-based composite activated carbon is 3.28mmol/g.
Subjecting the biomass-based composite activated carbon material to carbon dioxide adsorption analysis test 10 times by using the above 3H-2000PS2 type specific surface and pore size analyzer, wherein the adsorption process is determined by% 2 The analysis is carried out in the atmosphere and carried out at 200 DEG CAnd (3) row by row. 0.15g of adsorbent was packed in the test tube and the temperature was raised to 200 ℃ for 4 hours. The temperature was then reduced to 25 ℃ and adsorption was carried out under a carbon dioxide atmosphere. After the adsorption process is finished, the temperature is increased to 200 ℃, and the adsorbent is desorbed for 4 hours at 200 ℃. Then, the temperature is reduced to 25 ℃, the adsorption reaction is carried out again under the carbon dioxide atmosphere, and the process is repeated for 10 times. Under the condition, after 10 times of adsorption/desorption circulation processes, the adsorption capacity of the biomass-based composite activated carbon can still reach 3.276mmol/g, and the adsorption capacity is only reduced by 0.12%. The biomass-based composite activated carbon has better carbon dioxide adsorption cycle stability.
Finally, it should be noted that: the above examples are only intended to illustrate the technical solution of the present invention, and not to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, it should be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; and such modifications or substitutions do not depart from the spirit and scope of the corresponding technical solutions of the embodiments of the present invention.
Claims (5)
1. A preparation method of biomass-based activated carbon material is characterized by comprising the following steps: the activated carbon material comprises the following raw materials in parts by weight: 1 part of peony seed meal; 1-2 parts of fir bark;
the preparation method of the biomass-based activated carbon material comprises the following steps:
the method comprises the following steps: drying the peony seed meal and the cedar bark at 120 ℃, respectively, crushing to 300-500 meshes, and then mixing to obtain a mixed raw material A;
step two: mixing the mixed raw material A and the desulfurization waste liquid according to the solid-liquid ratio of 1g/5-20mL, performing ultrasonic impregnation for 2-6h under the condition of ultrasonic frequency of 25-40kHz, drying at 100-150 ℃, and performing carbonization and activation for 2-4h under the conditions of temperature of 500-700 ℃ and the temperature rise rate of carbonization and activation of 5-8 ℃/min, wherein the carbonization and activation are performed under the condition of air isolation; obtaining a mixed carbon material B;
step three: mixing the obtained mixed carbon material B with sodium amide according to the mass ratio of 1-2, and then isolating air to activate for 1.5-3h under the conditions that the temperature is 450-550 ℃ and the activation heating rate is 5-8 ℃/min, so as to obtain a biomass-based activated carbon material;
the total volume of micropores of the biomass-based activated carbon material is 0.52-1.25cm 3 /g。
2. A method of making a biomass-based activated carbon material as recited in claim 1, wherein: the specific surface area is 1033-2951cm 2 /g。
3. A method of making a biomass-based activated carbon material as recited in claim 1, wherein: the total pore volume is 0.57-1.60cm 3 /g。
4. A method of making a biomass-based activated carbon material as claimed in claim 1, characterised in that: the adsorption temperature is 0-50 deg.C, and the adsorption pressure is 0.01-0.1MPa.
5. A method of making a biomass-based activated carbon material as recited in claim 1, wherein: it is applied to adsorbing and capturing carbon dioxide.
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109354017A (en) * | 2018-10-17 | 2019-02-19 | 西安理工大学 | It is a kind of original position sulphur, nitrogen co-doped biomass carbon nanometer sheet preparation method |
| CN110723736A (en) * | 2019-07-12 | 2020-01-24 | 超威电源有限公司 | Biomass porous activated carbon material and preparation method and application thereof |
| CN111422865A (en) * | 2020-03-13 | 2020-07-17 | 西安交通大学 | Nitrogen-containing carbon material for supercapacitor and preparation method and application thereof |
| CN111453726A (en) * | 2019-08-12 | 2020-07-28 | 山东大学 | Nitrogen-doped porous carbon material and preparation method and application thereof |
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| KR102157515B1 (en) * | 2018-11-16 | 2020-09-18 | 한국세라믹기술원 | Manufacturing method of heteroatom-doped spherical porous active carbon and manufacturing method of the supercapacitor usig the porous active carbon |
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| CN109354017A (en) * | 2018-10-17 | 2019-02-19 | 西安理工大学 | It is a kind of original position sulphur, nitrogen co-doped biomass carbon nanometer sheet preparation method |
| CN110723736A (en) * | 2019-07-12 | 2020-01-24 | 超威电源有限公司 | Biomass porous activated carbon material and preparation method and application thereof |
| CN111453726A (en) * | 2019-08-12 | 2020-07-28 | 山东大学 | Nitrogen-doped porous carbon material and preparation method and application thereof |
| CN111422865A (en) * | 2020-03-13 | 2020-07-17 | 西安交通大学 | Nitrogen-containing carbon material for supercapacitor and preparation method and application thereof |
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