CN109422263B - Cellulose porous activated carbon and preparation method and application thereof - Google Patents
Cellulose porous activated carbon and preparation method and application thereof Download PDFInfo
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- CN109422263B CN109422263B CN201710718213.1A CN201710718213A CN109422263B CN 109422263 B CN109422263 B CN 109422263B CN 201710718213 A CN201710718213 A CN 201710718213A CN 109422263 B CN109422263 B CN 109422263B
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 108
- 229920002678 cellulose Polymers 0.000 title claims abstract description 91
- 239000001913 cellulose Substances 0.000 title claims abstract description 91
- 238000002360 preparation method Methods 0.000 title abstract description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 54
- 230000003213 activating effect Effects 0.000 claims abstract description 31
- 239000008247 solid mixture Substances 0.000 claims abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 28
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 27
- 239000000203 mixture Substances 0.000 claims abstract description 23
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 22
- 238000004108 freeze drying Methods 0.000 claims abstract description 19
- 239000007772 electrode material Substances 0.000 claims abstract description 18
- 238000002156 mixing Methods 0.000 claims abstract description 17
- 239000007864 aqueous solution Substances 0.000 claims abstract description 11
- 238000000227 grinding Methods 0.000 claims abstract description 11
- 239000002041 carbon nanotube Substances 0.000 claims abstract description 10
- 229910021393 carbon nanotube Inorganic materials 0.000 claims abstract description 10
- 239000000835 fiber Substances 0.000 claims abstract description 10
- 238000010000 carbonizing Methods 0.000 claims abstract description 8
- 239000011261 inert gas Substances 0.000 claims abstract description 8
- 235000015110 jellies Nutrition 0.000 claims abstract description 8
- 239000008274 jelly Substances 0.000 claims abstract description 8
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 159
- 238000000498 ball milling Methods 0.000 claims description 35
- 239000000463 material Substances 0.000 claims description 23
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims description 11
- 229920000742 Cotton Polymers 0.000 claims description 10
- 239000003792 electrolyte Substances 0.000 claims description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 4
- 244000025254 Cannabis sativa Species 0.000 claims description 2
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 claims description 2
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- 235000009120 camo Nutrition 0.000 claims description 2
- 235000005607 chanvre indien Nutrition 0.000 claims description 2
- 235000013399 edible fruits Nutrition 0.000 claims description 2
- 239000011487 hemp Substances 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- 239000010902 straw Substances 0.000 claims description 2
- 239000002023 wood Substances 0.000 claims description 2
- 235000005074 zinc chloride Nutrition 0.000 claims description 2
- 239000011592 zinc chloride Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 7
- 238000003763 carbonization Methods 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 14
- 239000003990 capacitor Substances 0.000 description 14
- 239000001768 carboxy methyl cellulose Substances 0.000 description 14
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 14
- 238000012360 testing method Methods 0.000 description 10
- 229910052799 carbon Inorganic materials 0.000 description 9
- 238000002474 experimental method Methods 0.000 description 9
- 238000003795 desorption Methods 0.000 description 8
- 238000001514 detection method Methods 0.000 description 8
- 238000001179 sorption measurement Methods 0.000 description 8
- 239000003575 carbonaceous material Substances 0.000 description 7
- 239000011148 porous material Substances 0.000 description 5
- 230000004913 activation Effects 0.000 description 4
- 239000000084 colloidal system Substances 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 239000005539 carbonized material Substances 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 229910021389 graphene Inorganic materials 0.000 description 3
- 230000008569 process Effects 0.000 description 3
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- 238000006243 chemical reaction Methods 0.000 description 2
- 238000002484 cyclic voltammetry Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000002336 sorption--desorption measurement Methods 0.000 description 2
- 239000012190 activator Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000007833 carbon precursor Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000001453 impedance spectrum Methods 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/24—Electrodes characterised by structural features of the materials making up or comprised in the electrodes, e.g. form, surface area or porosity; characterised by the structural features of powders or particles used therefor
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
- H01G11/40—Fibres
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
- H01G11/44—Raw materials therefor, e.g. resins or coal
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
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- C01P2006/16—Pore diameter
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
The invention relates to cellulose-based porous activated carbon and a preparation method and application thereof, wherein the method comprises the following steps: 1) mixing natural cellulose with an aqueous solution of an activating agent, fully grinding the mixture to obtain a fiber jelly, and freeze-drying the fiber jelly to obtain a solid mixture of the cellulose and the activating agent; 2) and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 500-1000 ℃ for 0.5-4 h to obtain the carbon nano tube. The invention also discloses application of the cellulose-based porous activated carbon in a supercapacitor electrode material. The method is simple to operate, and the use amount of the raw materials and the activating agent can be strictly controlled. The prepared porous activated carbon has extremely high specific surface area and can be widely applied to electrode materials of supercapacitors.
Description
Technical Field
The invention relates to the technical field of natural polymer materials, in particular to cellulose-based porous activated carbon and a preparation method and application thereof.
Background
The electrode material is used as a key part influencing the electric energy storage capacity (namely capacitance) of the super capacitor, and the research on the raw materials and the preparation method is particularly important for the characteristics of large specific surface area, good cycle characteristics and the like. Porous carbon materials have received much attention from researchers because of their advantages of availability, adjustable microstructure, and large specific surface area.
In recent years, many porous carbon materials have been studied including graphene, carbon nanotubes, biomass carbonized materials, and the like. Graphene and carbon nanotubes have good electrical conductivity and large specific surface area, but the preparation method is complex and expensive, which restricts the application of the graphene and carbon nanotubes. The biomass carbonized material has attracted the interest of many researchers with low price and abundant reserves, especially the biomass carbonized material obtained by chemical activation. The method is a main mode for preparing the electrode material of the super capacitor because the chemical activation is mild and simple, the yield is high, the pore size distribution of the obtained carbon material is clear and the specific surface area is high.
In the process of preparing the carbon material, the activation methods generally adopted are a soaking method and a hydrothermal method, and the amount of the activating agent entering the material is not uniform, and the reaction conditions are not precise, so that the prepared materials have certain difference.
Disclosure of Invention
The invention aims to provide a preparation method of cellulose-based porous activated carbon. The invention adopts a grinding mode to fully mix the natural cellulose raw material and the aqueous solution of the activating agent; not only simplifies the preparation method, but also effectively controls the reaction conditions and the use amount of the activating agent.
The method comprises the following steps:
1) mixing natural cellulose with an aqueous solution of an activating agent, fully grinding the mixture to obtain a fiber jelly, and freeze-drying the fiber jelly to obtain a solid mixture of the cellulose and the activating agent;
2) and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 500-1000 ℃ for 0.5-4 h to obtain the carbon nano tube.
The adopted natural cellulose has a macroscopic shape of fiber, particles or pulp; the mass percentage of cellulose in the natural cellulose is not less than 90%; the natural cellulose employed in the present invention is not limited in kind; preferably one or more of wood, cotton, hemp, crop straw or crop fruit.
The mode of purifying cellulose in the present invention is a conventional purification mode.
The activating agent is selected from one or more of potassium hydroxide, phosphoric acid or zinc chloride;
the mass ratio of the natural cellulose to the activating agent is 1: 0.2-2, and preferably 1: 0.6-1.6.
The weight percentage of the activating agent in the activating agent aqueous solution is 1 wt% -10 wt%, and preferably 3wt% -8 wt%.
When the activator of the present invention is an aqueous solution of potassium hydroxide, freeze drying removes the water leaving a solid potassium hydroxide and creating pores. In the carbonization process, at high temperature, potassium hydroxide reacts with carbon, and then the pore is formed by decomposition and gasification, so that the porous carbon material with large specific surface can be obtained.
In order to realize the full mixing of the natural cellulose and the potassium hydroxide aqueous solution, the grinding mode is adopted; further adopting a ball milling mode to fully and uniformly mix the raw materials with the aqueous solution of the activating agent; wherein, the grinding ball is made of one or more of zirconium dioxide, agate and steel ball; and/or the ball-to-feed ratio is 3-4: 1; and/or the ball milling time is 2-12 hours; and/or the rotating speed is 200-400 rpm.
The invention further adopts freeze drying after fully mixing. The temperature of the freeze drying is-60 ℃ to-100 ℃. Conventional drying causes shrinkage of the material without the structure of the sample being destroyed during freeze drying because the solid components are supported by the ice in their place. As the ice sublimes, voids remain in the dry residue, which preserves the chemical structural integrity of the product and creates voids.
The invention further provides that the step 2) is specifically as follows: and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 600-800 ℃ for 0.8-1.2 h to obtain the porous activated carbon.
As a preferred embodiment of the present invention, there is provided a method for producing a cellulose-based porous activated carbon, comprising the steps of:
1) mixing natural cellulose with 3-8 wt% of potassium hydroxide aqueous solution, ball-milling uniformly to obtain a fiber jelly, and freeze-drying at the temperature of-80 ℃ to obtain a solid mixture of the cellulose and the potassium hydroxide;
the mass ratio of the natural cellulose to the potassium hydroxide is 1: 0.6-1.6;
the mass percentage of cellulose in the natural cellulose is not less than 90%;
2) and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 600-800 ℃ for 0.8-1.2 h to obtain the carbon nano tube.
A second object of the present invention is to provide a cellulose-based porous activated carbon produced by any of the above-described methods.
The cellulose-based porous activated carbon has a specific surface area of 500m2/g~1000m2/g。
The third purpose of the invention is to provide the application of the cellulose-based porous activated carbon in the electrode material of the super capacitor;
the application specifically comprises the following steps: when the porous activated carbon is used as an electrode, a potassium hydroxide solution is used as an electrolyte.
Preferably, when the porous activated carbon is used as an electrode, a KOH solution with the concentration of 6mol/L is used as an electrolyte. The electrolyte has the advantages of high conductivity, low internal resistance, small ionic radius of the electrolyte, easy entry into micropores, full infiltration with the micropores, full utilization of the surface area of an electrode material and the like.
The invention has at least the following beneficial effects:
1. the invention adopts a ball milling mode to mix raw materials and an activating agent in one step, so that the raw materials and the activating agent are fully mixed; the method is simple to operate, and the use amount of the raw materials and the activating agent can be strictly controlled.
2. The fiber-based porous activated carbon prepared by the method has large specific surface area up to 1000m2(ii)/g, and is almost all microporous; as an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 300F/g at the highest under the current density of 1A/g, and the super capacitor has good cycle stability. The renewable, environment-friendly and low-cost cellulose is used as the active carbon precursor, and a new idea is provided for preparing the electrode material of the super capacitor through mixing and activation by a ball milling process.
Drawings
FIG. 1 is an SEM image of porous activated carbon prepared in example 1;
FIG. 2 is a nitrogen adsorption/desorption curve and a pore diameter distribution curve of porous activated carbon prepared in example 2;
FIG. 3 is a constant current charge and discharge diagram of porous activated carbon prepared in example 2;
FIG. 4 is a cyclic voltammogram of the porous activated carbon prepared in example 2;
FIG. 5 is an AC impedance spectrum of porous activated carbon prepared in example 2.
Detailed Description
The following examples are intended to illustrate the invention but are not intended to limit the scope of the invention.
Example 1
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 1.6g of potassium hydroxide into 18.4g of water, and mixing to obtain a mixture; wherein 1.6g of potassium hydroxide is added into 18.4g of water, and the concentration of the prepared potassium hydroxide solution is 8 wt%;
(2) preparing the mixture into cellulose gum by ball milling; wherein the ball milling tank and the grinding balls are made of zirconium dioxide, and the ball material ratio is 3.5: 1; ball milling is carried out for 10 hours at the rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
As shown in the SEM image of the porous carbon material of fig. 1, it is apparent from the figure that the material is indeed porous structure. The specific surface area of the obtained active carbon can reach 678 m through nitrogen adsorption and desorption experiment detection2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 180F/g under the current density of 1A/g.
Example 2
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 1g of potassium hydroxide into 19g of water, and mixing to obtain a mixture; wherein 1g of potassium hydroxide is added into 19g of water, and the concentration of the prepared potassium hydroxide solution is 5 wt%;
(2) preparing the mixture into cellulose gum by ball milling; wherein the ball milling tank and the grinding balls are made of zirconium dioxide, and the ball material ratio is 3.5: 1; ball milling is carried out for 10 hours at the rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. FIG. 2 shows the nitrogen adsorption/desorption curve and the pore size distribution curve of example 2, and the specific surface area of the obtained material is 1057m2(ii) in terms of/g. Fig. 3, fig. 4 and fig. 5 show the results of bipolar electrochemical performance tests of the activated carbon as an electrode material. The cyclic voltammetry curve of the porous carbon material is in a better rectangle-like shape, which shows the ideal double-layer capacitance characteristic, and the capacitance value and the internal resistance are obtained by constant current charge and discharge test and alternating current impedance test, the capacitance value reaches 290F/g, and the migration internal resistance is smaller and is only 0.90 omega.
Example 3
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 0.6g of potassium hydroxide into 19.4g of water, and mixing to obtain a mixture, wherein 0.6g of potassium hydroxide is added into 19.4g of water, and the concentration of the obtained potassium hydroxide solution is 3 wt%;
(2) preparing the mixture into cellulose gum by ball milling; wherein the ball milling tank and the grinding balls are made of zirconium dioxide, and the ball material ratio is 3.5: 1; ball milling is carried out for 10 hours at the rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. The specific surface area of the obtained active carbon can reach 960m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 194F/g under the current density of 1A/g.
Example 4
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 0.8g of potassium hydroxide into 19.2g of water, and mixing to obtain a mixture, wherein 0.8g of potassium hydroxide is added into 19.2g of water, and the concentration of the obtained potassium hydroxide solution is 4 wt%;
(2) preparing the mixture into cellulose gum by ball milling; wherein the ball milling tank and the balls are made of zirconium dioxide, the ball-material ratio is 3.5:1, and the ball milling is carried out for 10 hours at the rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon. SEM test proves that the material is really porous.
The specific surface area of the obtained active carbon can reach 842m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 178F/g under the current density of 1A/g.
Example 5
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 1.2g of potassium hydroxide into 18.8g of water, and mixing to obtain a mixture, wherein 1.2g of potassium hydroxide is added into 18.8g of water, and the concentration of the obtained potassium hydroxide solution is 6 wt%;
(2) preparing the mixture into cellulose gum by ball milling; wherein the ball milling tank and the balls are made of zirconium dioxide, the ball-material ratio is 3.5:1, and the ball milling is carried out for 10 hours at the rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. The specific surface area of the obtained active carbon can reach 898m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 152F/g under the current density of 1A/g.
Example 6
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 1.4g of potassium hydroxide into 18.6g of water, and mixing to obtain a mixture, wherein 1.4g of potassium hydroxide is added into 18.6g of water, and the concentration of the obtained potassium hydroxide solution is 7 wt%;
(2) preparing the mixture into cellulose colloid by ball milling, wherein the ball milling tank and balls are made of zirconium dioxide with a ball-to-material ratio of 3.5:1, and the ball milling is carried out for 10 hours at a rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. The specific surface area of the obtained active carbon can reach 906m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 143F/g under the current density of 1A/g.
Example 7
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 1g of potassium hydroxide into 19g of water, and mixing to obtain a mixture, wherein 1g of potassium hydroxide is added into 19g of water, and the concentration of the prepared potassium hydroxide solution is 5 wt%;
(2) preparing the mixture into cellulose colloid by ball milling, wherein the ball milling tank and balls are made of zirconium dioxide with a ball-to-material ratio of 3.5:1, and the ball milling is carried out for 10 hours at a rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 700 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. The specific surface area of the obtained active carbon can reach 663m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 120F/g under the current density of 1A/g.
Example 8
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of cotton pulp cellulose and 1g of potassium hydroxide into 19g of water, and mixing to obtain a mixture, wherein 1g of potassium hydroxide is added into 19g of water, and the concentration of the prepared potassium hydroxide solution is 5 wt%;
(2) preparing the mixture into cellulose colloid by ball milling, wherein the ball milling tank and balls are made of zirconium dioxide with a ball-to-material ratio of 3.5:1, and the ball milling is carried out for 10 hours at a rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 800 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. The specific surface area of the obtained active carbon can reach 510m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 103F/g under the current density of 1A/g.
Example 9
A method of making cellulose-based porous activated carbon, the method comprising the steps of:
(1) adding 1g of corncob cellulose and 1g of potassium hydroxide into 19g of water, and mixing to obtain a mixture, wherein 1g of potassium hydroxide is added into 19g of water, and the concentration of the prepared potassium hydroxide solution is 5 wt%;
(2) preparing the mixture into cellulose colloid by ball milling, wherein the ball milling tank and balls are made of zirconium dioxide with a ball-to-material ratio of 3.5:1, and the ball milling is carried out for 10 hours at a rotating speed of 300 rpm;
(3) freeze-drying the cellulose gum at-80 deg.C to obtain solid mixture of cellulose and potassium hydroxide;
(4) and (2) activating the solid mixture of carbonized cellulose and potassium hydroxide under the condition of nitrogen, wherein the carbonization temperature is 600 ℃, and the carbonization time is 1h, so as to obtain the cellulose-based porous activated carbon.
SEM test proves that the material is really porous. The specific surface area of the obtained active carbon can reach 910m through the detection of a nitrogen adsorption and desorption experiment2(ii) in terms of/g. As an electrode material of a super capacitor, the mass specific capacitance of a two-electrode system can reach 274F/g under the current density of 1A/g.
Although the invention has been described in detail hereinabove by way of general description, specific embodiments and experiments, it will be apparent to those skilled in the art that many modifications and improvements can be made thereto based on the invention. Accordingly, such modifications and improvements are intended to be within the scope of the invention as claimed.
Claims (12)
1. A method of making a cellulose-based porous activated carbon, comprising the steps of:
1) mixing natural cellulose with an aqueous solution of an activating agent, fully grinding the mixture to obtain a fiber jelly, and freeze-drying the fiber jelly to obtain a solid mixture of the cellulose and the activating agent; the activating agent is selected from one or more of potassium hydroxide, phosphoric acid or zinc chloride; the mass ratio of the natural cellulose to the activating agent is 1: 0.6-1.6; the weight percentage of the activating agent in the activating agent aqueous solution is 3-8 wt%;
the grinding is carried out in a ball milling mode; wherein, the grinding ball is made of one or more of zirconium dioxide, agate and steel ball; the ball-material ratio is 3-4: 1; the ball milling time is 2-12 hours, and the rotating speed is 200-400 rpm;
2) and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 500-1000 ℃ for 0.5-4 h to obtain the carbon nano tube.
2. The method according to claim 1, wherein the mass percentage of cellulose in the natural cellulose is not less than 90%.
3. The method of claim 2, wherein the natural cellulose is purified from one or more of wood, cotton, hemp, crop straw, or crop fruit.
4. The method according to any one of claims 1 to 3, wherein the temperature of the freeze drying is from-60 ℃ to-100 ℃.
5. The method according to any one of claims 1 to 3, wherein the step 2) is specifically: and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 600-800 ℃ for 0.8-1.2 h to obtain the carbon nano tube.
6. The method according to claim 4, wherein the step 2) is specifically: and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 600-800 ℃ for 0.8-1.2 h to obtain the carbon nano tube.
7. Method according to claim 1, characterized in that it comprises the following steps:
1) mixing natural cellulose with 3-8 wt% of potassium hydroxide aqueous solution, ball-milling uniformly to obtain a fiber jelly, and freeze-drying at the temperature of-80 ℃ to obtain a solid mixture of the cellulose and the potassium hydroxide;
the mass ratio of the natural cellulose to the potassium hydroxide is 1: 0.6-1.6;
the mass percentage of cellulose in the natural cellulose is not less than 90%;
2) and (2) putting the solid mixture prepared in the step 1) into an inert gas or nitrogen environment, and carbonizing at 600-800 ℃ for 0.8-1.2 h to obtain the carbon nano tube.
8. A cellulose-based porous activated carbon prepared by the method of any one of claims 1 to 7.
9. The cellulose-based porous activated carbon as claimed in claim 8, which has a specific surface area of 500m2/g~1000m2/g。
10. Use of a porous activated carbon as claimed in claim 8 or 9 in supercapacitor electrode materials.
11. The application according to claim 10, characterized in that it is specifically: the potassium hydroxide solution is used as the electrolyte.
12. Use according to claim 11, characterized in that a 6mol/L potassium hydroxide solution is used as electrolyte.
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