CN106672965A - Method for preparing high-surface-area multi-stage porous carbon with cotton straws - Google Patents

Method for preparing high-surface-area multi-stage porous carbon with cotton straws Download PDF

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CN106672965A
CN106672965A CN201710008199.6A CN201710008199A CN106672965A CN 106672965 A CN106672965 A CN 106672965A CN 201710008199 A CN201710008199 A CN 201710008199A CN 106672965 A CN106672965 A CN 106672965A
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activated carbon
cotton stalk
ratio surface
mesoporous activated
deionized water
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CN106672965B (en
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石勇
任铁真
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Xinjiang Hong Ruida Fiber Co Ltd
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Xinjiang Hong Ruida Fiber Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/12Surface area
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/14Pore volume
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/16Pore diameter

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Abstract

The invention belongs to the field of activated carbon and provides a method for preparing high-surface-area multi-stage porous carbon with cotton straws. The method includes: 1), pretreatment including (1) preparation of raw materials, namely smashing the cotton straws to be 5-15mm in particle size via or not via sheath-core separation and screening to remove residues; (2), rinsing with clean water, namely rinsing with water prior to dehydration; (3), rubbing and heap leaching, namely rubbing to devillicate after adding an alkalescent solution for heap leaching and extruding residual liquid for heap leaching; (4), bomb explosion treatment, namely putting into a sealed pressure vessel, pumping in high-pressure steam, keeping 1.0MPa-2.5MPa atmosphere pressure for 5-20 minutes, releasing materials and the steam in 60-75 millseconds and releasing the atmosphere pressure to normal pressure, and letting the materials to explode; (5), rinsing with deionized water, namely rinsing with the deionized water and performing dehydration; (6), performing drying; 2), adding of an ting agent; 3), drying and grinding; 4), activating; 5), washing; 6), drying. With the method, cotton straw carbon sources can be utilized, and the method is simple in process, small in use amount of the activating agent, low in production cost and suitable for promotion.

Description

A kind of method that cotton stalk prepares high-ratio surface multistage mesoporous activated carbon
Technical field
The invention belongs to activated carbon preparing technical field, specifically a kind of cotton stalk prepares high-ratio surface multi-stage porous activity The method of charcoal.
Background technology
Activated carbon is black powder or granular amorphous carbon, also the crystal carbon comprising marshalling.Activated carbon by Have that specific surface area is big in it, conduct electricity very well, electrochemical stability is good, high adsorption capacity the features such as, therefore be widely used In fields such as gas absorption separation, food processing, the electrode material of ultracapacitor, medical treatment, environmental protection, national defence, agriculturals.Activated carbon Preparation method be mainly natural material(Such as bagasse, cotton stalk, shell)After charing, then lived with activator mixing high temperature Change and obtain.It is cotton stalk to prepare the carbon source that activated carbon uses, and is the discarded object of agricultural product, not only increases the additional of agricultural product Value, and there are environment-friendly, wide material sources, with low cost, the specific surface area of the activated carbon for preparing is higher.But It is more single to be that activated carbon structure remains unchanged, and based on micropore, absorption property is poor, and preparation process consumes substantial amounts of activator.
The persursor material of activated carbon is prepared, two major classes are can be divided mainly at present:Plant and mineral substance.Plant is life Material, mainly has:Timber, stalk, cauline leaf, shell etc..Using the natural structure of biological material, micropore hair can be obtained Up to, specific surface area activated carbon very high, and with mechanical strength higher.Mineral substance raw material have:Coal, petroleum coke, synthesis Resin etc., in these raw material, coal resources are most abundant, but coal texture directly affects activated carbon with component characteristic Performance, ash content is high and is difficult to the flourishing micropore of generation.
By the use of renewable biomass, especially various biological materials are rich as activated carbon carbon matrix precursor material, raw material is prepared Richness, method is easy, economically feasible, environmentally friendly and endemic element that biological material can be utilized to possess in itself and structure. By corresponding process modification, people have been able to prepare the high-performance activity with unique texture using biological material Carbon, causes many researchs both domestic and external and concern.
Biological material is mainly and is grouped into by cellulose, hemicellulose and the great achievement of lignin three, but these three components exist Composition, structure in plant and distribution can be because of the species of plant, the place of production and growth period etc. it is different and different.Additionally, biomass In stalk also containing the organic compound such as a small amount of pectin, fat, wax and plant growth needed for, and transported and raw in raw material Various metallic elements brought during product etc..This causes that the chemical composition and structure of biomass straw are extremely complex, also causes There is very big difference in the pretreatment of different biomass straws and Land use systems, or even completely different.
At present, biological material is generally required when activated carbon is prepared as persursor material and pre-processed, its method Biological material is typically crushed to powder, its distinctive natural fine pore passage structure is not by corresponding technique hand Section is made full use of, therefore existing activated carbon from activated sludge technology of preparing solve only the Utilizing question of biological material, and The microscopic characteristics in the institutional framework of biological material are not made full use of, biomass microcellular structure and micropore surface is expanded Product.
Specific to cotton stalk, its content of lignin is higher than general biomass material, while ash content and gelatin substance content Height, makes it possess as the good natural endowment of activated carbon precursor, but have the shortcomings that to be more difficult to processing and utilization.
On the other hand, the preparation method of multistage mesoporous activated carbon mainly has template, chemical activation method and physically activated at present Method.Template is typically from a kind of material of special pore structure as template, import target material or presoma and make its Reacted in the hole of mould material, acted on using the limitation of mould material, realized anti-to the physics and chemistry in preparation process Should control, finally give the new material of structure-controllable.The pore structure and pattern of the multi-stage porous Carbon Materials that the method is obtained receive die The limitation of plate, and template preparation technology is relative complex, it is relatively costly.Physical activation method is first to be carbonized raw material, Ran Houzai Activated with vapor or carbon dioxide, the simple production process, cleaning, in the absence of asking for equipment corrosion and environmental pollution Topic, but activation temperature and soak time more long higher is generally needed, energy consumption is also higher.Chemical activation method is typically by general The presoma and activator of charcoal are mixed, then high-temperature calcination, can obtain specific surface area activated carbon higher, but can consume Substantial amounts of alkali activator, and have serious corrosivity to equipment.
China is large agricultural country, possesses abundant cotton stalk resource, and wherein most is idle to be wasted or on-site incineration, Cause serious air environmental pollution.
It is therefore desirable to study a kind of natural hole framework that can make full use of cotton stalk, process is simple, activator consumption Amount is few, realizes the method that low cost prepares high-specific surface area multistage mesoporous activated carbon.
The content of the invention
The purpose of the present invention be using it is cheap and easy to get and, environment-friendly cotton stalk, add by special pretreating process Work, the carbon source material of the microcosmic duct architecture for obtaining possessing excellent;A step activation method is used again, and with inorganic in activator Salt replaces a part of highly basic, and activator consumption is greatly lowered, equipment corrosion degree is also considerably reduced, so as to realize overcast Prepare high-ratio surface multistage mesoporous activated carbon.
The technical scheme is that:
A kind of method that cotton stalk prepares high-ratio surface multistage mesoporous activated carbon, implements according to the following steps:
Step one is pre-processed:Prepared including (1) raw material:By cotton stalk, separate and remove peach by core-skin, after leaf, withe The cladding and core material for obtaining crush the cladding and core material for obtaining 5~15mm of particle diameter respectively, or separate direct powder without core-skin It is broken, obtain the non-separating material of 5~15mm of particle diameter;Then the qualified material of 5~15mm of particle diameter is screened out, screening removes dust, miscellaneous Matter;(2) clear water rinsing:Material is rinsed with water, is then dehydrated;(3) dump leaching is rubbed:By heap after material addition weak caustic solution Leaching, machinery is rubbed to its sub-wire, extrudes surplus liquid, again dump leaching;(4) Hong quick-fried treatment:Material is inserted into closed pressure vessel It is interior, high steam is passed through, keep 1.0MPa~2.5MPa air pressure 5~20 minutes, discharge material and steam simultaneously in 60~75ms Pressure release to normal pressure, material is produced;(5) deionized water rinsing:Material is rinsed with deionized water, dehydration;(6) dry:By material Uniform drying;
Step 2 adds activator:Resulting material and the appropriate activator aqueous solution are sufficiently impregnated dissolving;
Step 3 drying grinding:It is ground into powder after moisture in material is removed;
Step 4 is activated:Material is carried out into activation heat treatment under nitrogen protective condition;
Step 5 is cleaned:Material is cleaned;
Step 6 is dried:Treatment is dried to material, high-ratio surface multistage mesoporous activated carbon is obtained final product.
Present invention additionally comprises optimization or/and improvement have:
One of preferred scheme:The activator aqueous solution in the step 2 is inorganic salts and the mixed solution of alkali;
The two of preferred scheme:Described activator is 2~3 with the consumption mass ratio of preceding material:7.5;
The three of preferred scheme:The temperature of the step 3 activation heat treatment is 800 DEG C, and the time is 1~2h;
The four of preferred scheme:Cleaning in the step 5 is respectively hydrochloric acid cleaning and deionized water cleaning.
Further preferred scheme has:
The five of preferred scheme:The activator aqueous solution in the step 2 is potassium carbonate and the mixed solution of potassium hydroxide;
The six of preferred scheme:Concentration of hydrochloric acid in the step 5 is 1mol/L.
Implementing the beneficial effect of technical solution of the present invention is:
The present invention prepares activated carbon using cotton stalk as carbon source material, belongs to the discarded object of agricultural product, not only increases agricultural production The added value of product, and there is environment-friendly, wide material sources, with low cost, the activated carbon specific surface area for preparing Higher, pore-size distribution is good;
The present invention can make full use of the natural fine pore passage structure of cotton stalk to be expanded into more by special pretreating process It is flourishing biomass microcellular structure so that the activated carbon of preparation can obtain bigger specific surface area and more flourishing hole point Cloth;
The present invention replaces a part of highly basic, activator consumption with inorganic salts in additionally using one-step preparation process, and activator It is greatly lowered, equipment corrosion degree is also considerably reduced, so as to realizes overcast local preparing high-ratio surface multistage mesoporous activated carbon.
To sum up, present invention process is simple, low production cost, good product quality, and sustainability is strong, is adapted to popularization and application.
Technical scheme is described in detail with reference to embodiment.
Brief description of the drawings
Nothing.
Specific embodiment
To make those skilled in the art more fully understand technical scheme, below with embodiment the present invention is made into One step ground is described in detail.
Embodiment 1
1.0t cottons stalk is taken as activated carbon precursor material, its step is:
Step one is pre-processed:(1) prepared by raw material:By cotton stalk, separate and remove peach by core-skin, obtain after leaf, withe Cladding and core material crush the cladding and core material for obtaining 5~15mm of particle diameter respectively, or separate directly crushing without core-skin, obtain To the non-separating material of 5~15mm of particle diameter;Then the qualified material of 5~15mm of particle diameter is screened out, screening removes dust, impurity;(2) Clear water is rinsed:Material is rinsed with water, is then dehydrated;(3) dump leaching is rubbed:By dump leaching, machine after material addition weak caustic solution Tool is rubbed to its sub-wire, extrudes surplus liquid, again dump leaching;(4) Hong quick-fried treatment:Material is inserted in closed pressure vessel, is led to Enter high steam, keep 1.0MPa~2.5MPa air pressure 5~20 minutes, discharge material and steam in 60~75ms and pressure release extremely Normal pressure, material is produced;(5) deionized water rinsing:Material is rinsed with deionized water, dehydration;(6) dry:Material is uniformly dried It is dry, obtain 0.3t pretreatment cotton stalks;
Step 2 adds activator:In mass ratio it is 1 by potassium hydroxide, potassium carbonate and the present embodiment pretreatment cotton stalk:2:7.5 Ratio mixing is dissolved in water, stirs, and the mixture is standing and soak for into 24h, is sufficiently impregnated pretreatment cotton stalk and aqueous slkali Dissolving;
Step 3 drying grinding:The mixture that will be obtained is placed in and 12h is dried in 100 DEG C of baking ovens, removes the moisture in mixture, obtains To product be ground into powder;
Step 4 is activated:The solid powder is placed in tube furnace, under nitrogen protection, is warmed up to the speed of 10 DEG C/min 100 DEG C, keep 1h, then be warmed up to 300 DEG C with the speed, speed now is set into 1 DEG C/min is warmed up to 400 DEG C, continue with The speed of 10 DEG C/min is warmed up to 800 DEG C, and keeps 2h, and room temperature is cooled under nitrogen atmosphere, obtains activation products;
Step 5 is cleaned:The activation products for obtaining first are cleaned with the HCl of 1mol/L, neutralized, by product deionized water after cleaning Clean to pH=7~8;
Step 6 is dried:Product after cleaning is dried into 12h in 100 DEG C of baking oven, high-specific surface area multistage mesoporous activated carbon is obtained 0.08t。
The absorbent charcoal material that the present embodiment is obtained is tested and analyzed through BJH computational methods, and the sample has micropore, mesoporous simultaneously With the hierarchical porous structure of macropore, and larger specific surface area is can obtain through step activation, specific surface area reaches 2398.6m2/g, hole Gap volume 1.727cm3/g, average pore size 2.925nm.
Embodiment 2
1.0t cottons stalk is taken as activated carbon precursor material, its step is:
Step one is pre-processed:(1) prepared by raw material:By cotton stalk, separate and remove peach by core-skin, obtain after leaf, withe 0.5t core materials are crushed to 5~15mm of particle diameter, and screening removes dust, impurity screening and removes dust, impurity, and particle diameter is more than into 15mm's Cladding is returned and continues to crush, and the unqualified material by size less than 5mm is discarded;(2) clear water rinsing:Material is floated with water Wash, be then dehydrated;(3) dump leaching is rubbed:By dump leaching after the NaOH weak caustic solutions of the pH9 of material addition 3% 48 hours, machinery was rubbed To its sub-wire, surplus liquid is extruded, again dump leaching 30 hours;(4) Hong quick-fried treatment:Material is inserted in closed pressure vessel, is led to Enter high steam, keep 2.0~2.5MPa air pressure 5~10 minutes, discharge material and steam in 60ms and pressure release is to normal pressure, thing Material is produced;(5) deionized water rinsing:Material is rinsed with deionized water, dehydration;(6) dry:Material is uniformly dried, is obtained 0.35t pre-processes cotton stalk;
Step 2 adds activator:In mass ratio it is 1 by potassium hydroxide, potassium carbonate and the present embodiment pretreatment cotton stalk:2:7.5 Ratio mixing is dissolved in water, stirs, and the mixture is standing and soak for into 24h, is sufficiently impregnated cotton stalk cladding and aqueous slkali molten Solution;
Step 3 drying grinding:The mixture for obtaining is placed in and 12h is dried in 100 DEG C of baking ovens, removes the moisture in mixture, obtains Product be ground into powder;
Step 4 is activated:The solid powder is placed in tube furnace, under nitrogen protection, is warmed up to the speed of 10 DEG C/min 100 DEG C, keep 1h, then be warmed up to 300 DEG C with the speed, speed now is set into 1 DEG C/min is warmed up to 400 DEG C, continue with The speed of 10 DEG C/min is warmed up to 800 DEG C, and keeps 2h, and room temperature is cooled under nitrogen atmosphere, obtains activation products;
Step 5 is cleaned:The activation products for obtaining first are cleaned with the HCl of 1mol/L, neutralized, by product deionized water after cleaning Clean to pH=7~8;
Step 6 is dried:Product after cleaning is dried into 12h in 100 DEG C of baking oven, high-specific surface area multistage mesoporous activated carbon is obtained 0.1t。
The absorbent charcoal material that the present embodiment is obtained is tested and analyzed through BJH computational methods, and the sample has micropore, mesoporous simultaneously With the hierarchical porous structure of macropore, and larger specific surface area is can obtain through step activation, specific surface area reaches 2261.1m2/g, hole Gap volume 1.641cm3/g, average pore size 2.903nm.
Embodiment 3
1.0t cottons stalk is taken as activated carbon precursor material, its step is:
Step one is pre-processed:(1) prepared by raw material:Take a certain amount of cotton stalk, without core-skin separate, be directly crushed to particle diameter 5~ Chalk dust removing, impurity are removed in 15mm, screening;(2) clear water rinsing:Material is rinsed, is dehydrated to water content about;(3) dump leaching is rubbed: By dump leaching after the NaOH weak caustic solutions of the pH9.5 of material addition 1% 48 hours, machinery was rubbed to its sub-wire, extrudes surplus liquid, Dump leaching 42 hours again;(4) Hong quick-fried treatment:Material is inserted in closed pressure vessel, high steam is passed through, 1.0MPa gas is kept Pressure 5 minutes, discharges material and steam and pressure release is to normal pressure with the time of 60ms, and material is produced;(5) deionized water rinsing:By thing Material is rinsed with deionized water, dehydration;(6) dry:Material is uniformly dried, 0.7t pretreatment cotton stalks are obtained;
Step 2 adds activator:In mass ratio it is 1 by potassium hydroxide, potassium carbonate and the present embodiment pretreatment cotton stalk:2:7.5 Ratio mixing is dissolved in water, stirs, and the mixture is standing and soak for into 24h, is sufficiently impregnated pretreatment cotton stalk and aqueous slkali Dissolving;
Step 3 drying grinding:The mixture that will be obtained is placed in and 12h is dried in 100 DEG C of baking ovens, removes the moisture in mixture, obtains To product be ground into powder;
Step 4 is activated:The solid powder is placed in tube furnace, under nitrogen protection, is warmed up to the speed of 10 DEG C/min 100 DEG C, keep 1h, then be warmed up to 300 DEG C with the speed, speed now is set into 1 DEG C/min is warmed up to 400 DEG C, continue with The speed of 10 DEG C/min is warmed up to 800 DEG C, and keeps 2h, and room temperature is cooled under nitrogen atmosphere, obtains activation products;
Step 5 is cleaned:The activation products for obtaining first are cleaned with the HCl of 1mol/L, neutralized, by product deionized water after cleaning Clean to pH=7~8;
Step 6 is dried:12h will be dried in the baking oven of 100 DEG C of product after cleaning, obtain high-specific surface area multistage mesoporous activated carbon 0.2t。
The absorbent charcoal material that the present embodiment is obtained is tested and analyzed through BJH computational methods, and the sample has micropore, mesoporous simultaneously With the hierarchical porous structure of macropore, and larger specific surface area is can obtain through step activation, specific surface area reaches 1963.3m2/g, hole Gap volume 1.415cm3/g, average pore size 2.88nm.
It is understood that the above example principle being intended to be merely illustrative of the present and the exemplary embodiment party for using Formula, but the invention is not limited in this, implementer can technology according to the present invention scheme and actual conditions combination known technology To determine specific embodiment.For those skilled in the art, spirit of the invention and reality are not being departed from In the case of matter, various changes and modifications can be made therein, and increased these variations and modifications are also considered as protection scope of the present invention.

Claims (7)

1. a kind of method that cotton stalk prepares high-ratio surface multistage mesoporous activated carbon, it is characterised in that comprise the following steps:
Step one is pre-processed:Prepared including (1) raw material:By cotton stalk, separate and remove peach by core-skin, after leaf, withe The cladding and core material for obtaining crush the cladding and core material for obtaining 5~15mm of particle diameter respectively, or separate direct powder without core-skin It is broken, obtain the non-separating material of 5~15mm of particle diameter;Then the qualified material of 5~15mm of particle diameter is screened out, screening removes dust, miscellaneous Matter;(2) clear water rinsing:Material is rinsed with water, is then dehydrated;(3) dump leaching is rubbed:By heap after material addition weak caustic solution Leaching, machinery is rubbed to its sub-wire, extrudes surplus liquid, again dump leaching;(4) Hong quick-fried treatment:Material is inserted into closed pressure vessel It is interior, high steam is passed through, keep 1.0MPa~2.5MPa air pressure 5~20 minutes, discharge material and steam simultaneously in 60~75ms Pressure release to normal pressure, material is produced;(5) deionized water rinsing:Material is rinsed with deionized water, dehydration;(6) dry:By material Uniform drying;
Step 2 adds activator:Resulting material and the appropriate activator aqueous solution are sufficiently impregnated dissolving;
Step 3 drying grinding:It is ground into powder after moisture in material is removed;
Step 4 is activated:Material is carried out into activation heat treatment under nitrogen protective condition;
Step 5 is cleaned:Material is cleaned;
Step 6 is dried:Treatment is dried to material, high-ratio surface multistage mesoporous activated carbon is obtained final product.
2. the method that a kind of cotton stalk according to claim 1 prepares high-ratio surface multistage mesoporous activated carbon, its feature exists In the activator aqueous solution in the step 2 is inorganic salts and the mixed solution of alkali.
3. the method that a kind of cotton stalk according to claim 2 prepares high-ratio surface multistage mesoporous activated carbon, its feature exists In the activator aqueous solution in the step 2 is potassium carbonate and the mixed solution of potassium hydroxide.
4. the method that a kind of cotton stalk according to claim 1 prepares high-ratio surface multistage mesoporous activated carbon, its feature exists In activator and the mass ratio of material are 2~3 in the step 2:7.5.
5. the method that a kind of cotton stalk according to claim 1 prepares high-ratio surface multistage mesoporous activated carbon, its feature exists In the temperature of the step 3 activation heat treatment is 800 DEG C, and the time is 1~2h.
6. the method that a kind of cotton stalk according to claim 1 prepares high-ratio surface multistage mesoporous activated carbon, its feature exists In the cleaning in the step 5 is respectively hydrochloric acid cleaning and deionized water cleaning.
7. the method that a kind of cotton stalk according to claim 6 prepares high-ratio surface multistage mesoporous activated carbon, its feature exists In the concentration of hydrochloric acid in the step 5 is 1mol/L.
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CN109037677A (en) * 2017-06-12 2018-12-18 四川大学 A kind of porous carbon negative pole material of lithium ion battery and preparation method thereof
CN109192540A (en) * 2018-09-18 2019-01-11 中联西北工程设计研究院有限公司 A kind of biomass carbonization product and manganese dioxide composite electrode material and preparation method thereof
CN110422837A (en) * 2019-08-02 2019-11-08 新疆弘瑞达纤维有限公司 A method of fluorescent carbon point is prepared using biomass material
CN111617737A (en) * 2019-02-27 2020-09-04 河北工业大学 Hierarchical porous carbon material and preparation method and application thereof
CN114804098A (en) * 2022-03-18 2022-07-29 广东省农业科学院作物研究所 Method for preparing porous activated carbon by adopting waste tobacco straws
CN115784227A (en) * 2022-11-07 2023-03-14 河南农业大学 Method for preparing porous carbon from agriculture and forestry biomass

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CN102586897A (en) * 2011-12-21 2012-07-18 中国热带农业科学院海口实验站 Method for preparing banana cellulose nanofibers by using steam explosion technology

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CN101112983A (en) * 2007-06-08 2008-01-30 山东大学 Preparation method of mizue brocade straw activated charcoal
CN101423213A (en) * 2007-10-30 2009-05-06 山东科技大学 Method for preparing active carbon
CN102586897A (en) * 2011-12-21 2012-07-18 中国热带农业科学院海口实验站 Method for preparing banana cellulose nanofibers by using steam explosion technology

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109037677A (en) * 2017-06-12 2018-12-18 四川大学 A kind of porous carbon negative pole material of lithium ion battery and preparation method thereof
CN109192540A (en) * 2018-09-18 2019-01-11 中联西北工程设计研究院有限公司 A kind of biomass carbonization product and manganese dioxide composite electrode material and preparation method thereof
CN111617737A (en) * 2019-02-27 2020-09-04 河北工业大学 Hierarchical porous carbon material and preparation method and application thereof
CN110422837A (en) * 2019-08-02 2019-11-08 新疆弘瑞达纤维有限公司 A method of fluorescent carbon point is prepared using biomass material
CN114804098A (en) * 2022-03-18 2022-07-29 广东省农业科学院作物研究所 Method for preparing porous activated carbon by adopting waste tobacco straws
CN114804098B (en) * 2022-03-18 2024-02-06 广东省农业科学院作物研究所 Method for preparing porous activated carbon from waste tobacco straw
CN115784227A (en) * 2022-11-07 2023-03-14 河南农业大学 Method for preparing porous carbon from agriculture and forestry biomass

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