CN104891479B - Plant-based graphene and preparation method thereof - Google Patents

Plant-based graphene and preparation method thereof Download PDF

Info

Publication number
CN104891479B
CN104891479B CN201510275731.1A CN201510275731A CN104891479B CN 104891479 B CN104891479 B CN 104891479B CN 201510275731 A CN201510275731 A CN 201510275731A CN 104891479 B CN104891479 B CN 104891479B
Authority
CN
China
Prior art keywords
graphene
preparation
catalyst
base class
plant
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510275731.1A
Other languages
Chinese (zh)
Other versions
CN104891479A (en
Inventor
孙康
蒋剑春
陈超
邓先伦
卢辛成
朱光真
贾羽洁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Institute of Chemical Industry of Forest Products of CAF
Original Assignee
Institute of Chemical Industry of Forest Products of CAF
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Institute of Chemical Industry of Forest Products of CAF filed Critical Institute of Chemical Industry of Forest Products of CAF
Priority to CN201510275731.1A priority Critical patent/CN104891479B/en
Publication of CN104891479A publication Critical patent/CN104891479A/en
Application granted granted Critical
Publication of CN104891479B publication Critical patent/CN104891479B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention provides plant-based graphene and a preparation method thereof. The preparation method comprises the steps of liquefying and filtering plant raw materials to obtain biological oil; mixing the biological oil with a catalyst to obtain a mixture, placing the mixture into a self-pressurizing reactor, sealing the reactor, catalytically calcining for 1 to 12 hours at the temperature of 500 to 1200 DEG C, cooling, washing by utilizing hydrochloric acid to remove the catalyst, rinsing by utilizing deionized water, and drying to obtain the quasi-graphene. According to the preparation method, the plant raw materials are firstly liquefied into biological oil which mainly includes oligosaccharide and a phenolic substance, then the biological oil is mixed with the catalyst, and under the high temperature and high pressure, the biological oil is converted to quasi-graphene on the surface of the catalyst, so that a novel method for preparing the quasi-graphene material in a mass manner by virtue of cheap plant raw materials is provided.

Description

Plant base class Graphene and preparation method thereof
Technical field
The present invention relates to plant base class grapheme material and preparation method thereof and in particular to plant resourceses through liquefaction, low Warm catalysis calcination prepares the industrial method of super capacitor active carbon composite.
Background technology
Graphene (graphene) is a kind of two dimension material with carbon element, is single-layer graphene, bilayer graphene and few layer graphene General designation.Graphene is the thinnest, the hardest nano material in known world, and it also has, and specific surface is big, and conductivity is high, heating power Learn the feature of function admirable, all can play an important role in life science and energy field.At present, prepare Graphene Method has graphite oxide reducing process, epitaxial growth method, chemical vapour deposition technique, mechanical stripping method, electrochemical method.Graphite oxide Reducing process adopts the thinking of reduction after initial oxidation, comprises the concrete steps that and first prepares graphite oxide, then with methods such as ultrasound wave, thermal expansions Graphene oxide is stripped out as far as possible, finally graphene oxide is changed into by Graphene using suitable reducing agent, such as adopt Hydrazine hydrate reduces to graphene oxide, and the carbon atom that wherein hybrid form is sp3 is changed into sp2 carbon network lattice composition Graphene.Carbon is entrained in formation interstitial impurity in rare metal with the method for seeping at high temperature by epitaxial growth method, then with K cryogenic treatment makes carbon in metal substrate surface indigenous graphite alkene epitaxial.When the first layer graphene is not yet completely covered metal substrate When, the second layer has begun to grow, because ground floor is entirely different with the chemical key class of the second layer graphene and metal substrate, Gap between weakness coupling and powerful covalent bond effect makes the second layer graphene be easy to be stripped out.Chemistry Vapour deposition process, with metal single crystal as substrate, is reached accurately by changing temperature, regulation substrate, exposed amount of control predecessor etc. Control the purpose of graphene film thickness.Concrete mode is the thick ni film of 300mm to be heated to after 1000 degrees Celsius be exposed to first In alkane atmosphere, thus forming highly purified graphene film on ni surface.Micromechanics partition method micromechanics partition method is most original Stripping Graphene method.During concrete operations, make graphite expansion in order to separate frequently with some way, mono-layer graphite can not Regular occurs in graphite surface, and this method is compared chemical stripping method and is more difficult to control to Graphene form, is unsuitable for high-precision Degree commercial production.
Yang Rong et al. disclose the conductive carbon material of a species graphene-structured preparation method (application number: 201410134804.0), meerschaum powder, sucrose are mixed homogeneously with deionized water, then ultrasonic disperse, then microwave heating, Mass fraction be 98.3% concentrated sulphuric acid exsiccator in place 24-144h;In this step, sucrose heated by microwave is converted into Caramel.Carry out carbonization, caramel carbonization in meerschaum layered framework in protective gas atmosphere.Meerschaum after carbonization is adopted Alternately it is acidified washing with Fluohydric acid., hydrochloric acid, then using the clean meerschaum of deionized water and fully dry, obtain class graphene-structured Conductive carbon material.
Burnt odd-prescription (burnt odd-prescription, the preparation of class graphene carbon nanometer fragment and its electrocatalysis characteristic, [academic dissertation], south China Normal university, 2013) with waste and old lithium ion battery Carbon anode as raw material, through a series of pre-treatment-chemical oxidation-ultrasound wave Pulverizing-dialysis purification etc. is processed, and obtains oxidation state carbon nanometer fragment, result shows: oxidation state carbon nanometer fragment contour is coarse, thick Spend for 1.5nm, profile is similar to Graphene, size is from 5nm~2 μm, and contains substantial amounts of oxygen-containing functional group and defect.
Zhu Runliang etc. discloses the preparation method (publication number of the nano-carbon material of a species graphene-structured cn103058168a).The bentonite having adsorbed dyestuff is dried successively, pulverizes, carbonization, acidifying washing, be dried, obtain class The nano-carbon material of graphene-structured.This invention, with discarded bentonite as raw material, prepares one kind and has large specific surface area Novel nano stratiform material with carbon element, simultaneously for solving bentonitic resource after absorbing dye and recycling to provide new way, Achieve the bentonite resourceization after wastewater treatment to utilize, thus contributing to promoting bentonite in dyestuff/treatment of dyeing wastewater Application.
Zhou Xufeng discloses a kind of preparation method of Graphene and Graphene patent of invention (publication number cn104477901a). Metallic catalyst is mixed with water, obtains the aqueous solution of metallic catalyst;Aqueous solution by gel like material and metallic catalyst Mixing, obtains the hydrogel material being adsorbed with metallic catalyst, described gel like material includes starchy compounds, cellulose family One or more of compound and synthetic resin;The hydrogel material being adsorbed with metallic catalyst is in protective gas atmosphere or true Carry out heat treatment under Altitude, obtain Graphene.
Liang Xuelei etc. (Liang Xuelei, Li Wei, guangjun c etc. the impact of the Graphene quality that transfer process grows to cvd [j]. Science Bulletin, 2014, (33)) Graphene that grown on the metallic substrate using the chemical vapor sedimentation method (cvd).Using drawing Graceful spectrum and x-ray photoelectron spectroscopy (xps) demonstrate metallic substrates corrosive liquid in transfer process and can introduce in graphenic surface Pollution, using " rca (radio corporation of america) cleaning (the modified rca of improvement of our development Clean) " shifting process can remove this pollution effectively, and this has important to the performance of the electronic device improving follow-up preparation Meaning.
Positive light of Guilin University of Technology Zou etc. [Zou Zhengguang, Yu Huijiang, Long Fei, etc. ultrasonic wave added hummers method prepares go [j]. Chinese Journal of Inorganic Chemistry, 2011,27 (09): 1753-1757.] low temperature to hummers method (≤10 DEG C), middle temperature respectively (38 DEG C) and low middle thermophase carry out the ultrasonic wave added of different capacity, explore the impact to hummers method for the ultrasound wave.They send out Existing go interlamellar spacing is descending to be followed successively by low middle temperature ultrasonic wave added, middle temperature ultrasonic wave added, low temperature ultrasonic auxiliary.Moreover, stone Black alkene interlamellar spacing becomes positive correlation with ultrasonic power, and spacing is conducive to more greatly monolayer go to peel off it is possible to according to different experiments need Ask and prepare monolayer go or intercalation go.
Jia Qina etc. [Jia Qina, Zhao Guangchao. the preparation of Graphene solid-phase micro-extraction fibre and the detection to Polychlorinated biphenyls [j]. analysis test journal, 2013,32 (05): 541-546.] will be molten for the titanium adding Graphene by solid phase micro-extraction technique Fiber made by glue-gel, makes this fiber have all of advantage of both Graphene and gel, not only possesses quite high specific surface Long-pending, stronger heat stability and excellent mechanical strength, and have three dimensional structure to provide more adsorption sites.
[critical process of Ren little Meng, Wang Yuansheng, He Te .hummers method synthesizing graphite alkene and the reaction mechanism such as Ren little Meng [j]. material engineering, 2013 (01): 1-5.] classical hummers method is probed into, during by changing its reaction temperature, temperature control Between, the amount of reacting substance etc. respectively each group product being detected.Find the optimal temperature in the low-temp reaction stage of hummers method Degree is that the response time can suitably increase close to 0 DEG C, and the concentrated sulphuric acid in the low-temp reaction stage and potassium permanganate can excessively add, The addition of sodium nitrate does not interfere with reaction substantially, and the temperature of middle thermophase is adjusted to as 30~45 DEG C, and the response time increases 90min is best, ensures that with this oxidation of graphite is more deep, and lamella peels off more complete.But the most impact yield Temperature rise period, this seminar finds to be maximum output scope in 90~100 DEG C by temperature control, is gone by repeatedly a small amount of addition Ionized water, and the response time should be shortened as far as possible, prevent product from reuniting again.
Although above method successfully prepares high-quality Graphene, preparation process is with high costs, pollution is big, is difficult to Industrialization.Therefore, macroblock quantization production and large scale produce to remain and hinder grapheme material to put into the main of commercialization on a large scale Bottleneck.At present, there is not yet the preparation method of plant base thunder grapheme material is reported, biomass scale liquefaction technology is ripe, Therefore, with the low plant base of wide material sources, degree of crystallinity as raw material, class grapheme material is prepared by liquefaction and catalysis calcination, can Realize extensive industrialization, cost is greatly reduced, and environmental pollution is little, product dispersive property more preferably, is more easy to store.
Content of the invention
Preparation process magnanimity preparation in order to solve prior art presence is difficult, seriously polluted, the problems such as expensive, this Invention puies forward a kind of plant base liquefied catalytic preparation class grapheme material and its method, can achieve extensive industrialization, preparation process Cleaning, step is simple, low cost of manufacture, and product dispersive property more preferably, is more easy to store.
The technical scheme is that the preparation method of plant base class Graphene, comprise the steps:
The first step, plant is liquefied: agricultural-forestry biomass raw material and the phenol of drying is liquefied, filters and remove inorganic impurity After obtain bio oil;
Second step, bio oil is mixed with catalyst: with iron series element nitrate as catalyst, catalyst and bio oil according to Mass ratio (0.1~1.0) 1.0 is mixed;
3rd step, seals pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is less than anti- Answer body amass 1/3, carry out airtight pretreatment;
4th step, calcining: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, heat up calcining, treats that calcining terminates Afterwards, natural cooling, takes out sample, reclaims catalyst through pickling, and deionized water rinses, after being dried, as described plant base class Graphene sample, electrical conductivity 370s/cm of plant base class Graphene, specific surface area 760m2/ g, thickness 1-3nm.
Plant material described in the first step includes wood flour, bamboo scraps, straw, dries and uses.
Bio oil described in the first step removes solid impurity through filtering off.
In second step, iron series element includes ferrum, nickel, cobalt.
In second step, iron series element nitrate is at the uniform velocity stirred when being mixed with bio oil.
In 4th step, calcining heat is 500~1200 DEG C, calcination time 1-10h.
The Graphene that the preparation method of described plant base class Graphene obtains, electrical conductivity 180~370s/cm, specific surface area 420~760m2/ g, thickness 1-3nm.
The yield of plant base class grapheme material of the present invention, specific surface area, thickness can be by catalyst loadings, activation temperature Degree, calcining heat and time control.The preparation of plant base class grapheme material: the plant material of drying and phenol are carried out liquid Change, filter and obtain bio oil after removing inorganic impurity.Bio oil is mixed with catalyst: with iron series element nitrate as catalyst, Mixed according to mass ratio (0.1~1.0) 1.0 with bio oil.A certain amount of said mixture is placed in spontaneous pressure reactor Interior, inventory is less than the 1/3 of reactor volume, carries out airtight pretreatment.The spontaneous pressure reactor that will be equipped with material is placed in height In warm stove, it is warming up to 500-1200 DEG C with certain heating rate, keep 1-10h.After calcining terminates, natural cooling, takes out sample Product, reclaim catalyst through pickling, and deionized water rinses, after being dried, as described class Graphene sample.Plant base class Graphene Electrical conductivity 180~370s/cm, specific surface area 420~760m2/ g, thickness 1-3nm.
Beneficial effect:
1. first plant base raw material is liquefied pretreatment.Plant base raw material reduces the crystallization of Plant fiber by liquefaction process Degree, obtains oligosaccharide and aldehydes matter, reduces graphited activation energy, improves graphitization conversion ratio.And liquefaction technology equipment Realize industrialization, acquisition can prepare the raw material of Graphene on a large scale.
2. catalyzed graphitization prepares grapheme material.Load Fe-series catalyst, in spontaneous pressure, can obviously reduce graphitization Temperature, improves Graphene yield.Electrical conductivity 370s/cm of plant base class Graphene, specific surface area 760m2/ g, thickness 1-3nm.
Brief description
Fig. 1 is the embodiment of the present invention 1 plant Graphene electron microscope.
Fig. 2 is the xrd figure of embodiment 1.
Fig. 3 is the atomic force microscopy figure of embodiment 1.
Fig. 4 is the schematic diagram of spontaneous pressure reactor.
1 is resistance furnace, and 2 is thermocouple, and 3 is resistance wire, and 4 is electrically heated rod, and 5 is rustless steel hermetically sealed can, and 6 is blow vent.
Specific embodiment
The present invention is as follows to the method for testing of prepared plant base class grapheme material performance:
(1) specific area measuring: using the mensure to nitrogen adsorption isotherm for the activated carbon under the conditions of liquid nitrogen, public according to bet Formula calculates specific surface area.
(2) surface topography is using projection Electronic Speculum (tem) and atomic force microscope (afm) test.
(3) conductance measurement: szt-c type four Probe test station measures.
The preparation method of plant base class Graphene, comprises the steps:
The first step, plant is liquefied: the plant material of drying and phenol is liquefied, filters and obtain after removing inorganic impurity Bio oil.Plant material is converted into by bio oil by liquefaction, composition is mainly oligosaccharide and aldehydes matter.This step can be joined Kao Wangyuan garden, Ye Lei, Shen Huyan, etc. Caulis Zizaniae caduciflorae abandoned biomass Liquefaction Products in Phenol and its product resin prepare adhesive [j]. and wide State chemical industry, 2014, (23).;Li Gaiyun, Zhu Xianchao, Zou Xianwu, etc. the quick Liquefaction Products in Phenol of microwave-assisted poplar and Characterization of The Products [j]. forest-science, 2014, (11) .doi:doi:10.11707/j.1001-7488.20141116.;Sun Fengwen, Li little Ke. Bamboo wood Liquefaction Products in Phenol and adhesive preparation technology [j]. chemistry of forest product and industry, 2007,27 (6): 65-70.doi:doi: 10.3321/j.issn:0253-2417.2007.06.014.;Take off refined person of outstanding talent, Zhang Qiuhui, Li Jianzhang. Lignum seu Ramulus Cunninghamiae Lanceolatae Liquefaction Products in Phenol thing synthesizes The research [j] of thermoset phenolic resin. biomass Chemical Engineering, 2007,41 (5): 9-12.doi:doi:10.3969/ j.issn.1673-5854.2007.05.003.;Qin Tefu, Luo Bei, Li Gaiyun. the Liquefaction Products in Phenol of artificial forest wood and resinification Research. the preparation of liquefied wood base phenolic resin and performance characterization [j]. timber industry, 2006,20 (5): 8-10.doi:doi: 10.3969/j.issn.1001-8654.2006.05.003.;Ma Xiaojun, Zhao Guangjie. it is fine that Wood Liquefaction Products in Phenol product prepares carbon The Primary Study [j] of dimension. chemistry of forest product and industry, 2007,27 (2): 29-32.doi:doi:10.3321/j.issn:0253- 2417.2007.02.007. the method described in.
Second step, bio oil is mixed with catalyst: with iron series element nitrate as catalyst, with bio oil according to mass ratio (0.1~1.0) 1.0 is mixed.
3rd step, seals pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is less than anti- Answer body amass 1/3, carry out airtight pretreatment.
4th step, calcining: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, is warming up to certain heating rate 500-1200 DEG C, keep 1-10h.After calcining terminates, natural cooling, takes out sample, reclaims catalyst through pickling, use deionization Water rinses, after being dried, as described class Graphene sample.Electrical conductivity 370s/cm of plant base class Graphene, specific surface area 760m2/ g, thickness 1-3nm.
Plant material described in the first step includes wood flour, bamboo scraps, the agricultural-forestry biomass raw material such as straw, needs drying and processing.
Bio oil described in the first step need to remove solid impurity through filtering off.
In second step, iron series element includes ferrum, nickel, cobalt.
In second step, iron series element nitrate is at the uniform velocity stirred when being mixed with bio oil.
Described spontaneous pressure reaction unit is outer layer is resistance furnace 1, sets rustless steel hermetically sealed can 5, resistance furnace 1 in resistance furnace 1 Inside it is provided with resistance wire 3, spontaneous pressure reactor is heated by electrically heated rod 4, monitors temperature, resistance furnace 1 by the interior thermocouple 2 setting It is additionally provided with blow vent 6.
Embodiment 1
(1) plant liquefaction: the bamboo scraps of drying and phenol are liquefied, obtains bio oil through filtering off except inorganic impurity.
(2) bio oil is mixed with catalyst: with nickel nitrate as catalyst, carries out according to mass ratio 0.1 1.0 with bio oil Mixing.
(3) seal pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is reactor volume 1/3, carry out airtight pretreatment.
(4) calcine: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, is warming up to 500 with certain heating rate DEG C, keep 1h.After calcining terminates, natural cooling, takes out sample, reclaims catalyst through pickling, deionized water rinses, be dried Afterwards, as described class Graphene sample.Electrical conductivity 180s/cm of plant base class Graphene, specific surface area 420m2/ g, thickness 1- 3nm.
Embodiment 2
(1) plant liquefaction: the bamboo scraps of drying and phenol are liquefied, obtains bio oil through filtering off except inorganic impurity.
(2) bio oil is mixed with catalyst: with nickel nitrate as catalyst, carries out according to mass ratio 1.0 1.0 with bio oil Mixing.
(3) seal pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is reactor volume 1/3, carry out airtight pretreatment.
(4) calcine: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, is warming up to 1200 with certain heating rate DEG C, keep 10h.After calcining terminates, natural cooling, takes out sample, reclaims catalyst through pickling, deionized water rinses, do After dry, as described class Graphene sample.Electrical conductivity 327s/cm of plant base class Graphene, specific surface area 590m2/ g, thickness 1-3nm.
Embodiment 3
(1) plant liquefaction: the bamboo scraps of drying and phenol are liquefied, obtains bio oil through filtering off except inorganic impurity.
(2) bio oil is mixed with catalyst: with nickel nitrate as catalyst, carries out according to mass ratio 0.7 1.0 with bio oil Mixing.
(3) seal pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is reactor volume 1/3, carry out airtight pretreatment.
(4) calcine: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, is warming up to 1100 with certain heating rate DEG C, keep 10h.After calcining terminates, natural cooling, takes out sample, reclaims catalyst through pickling, deionized water rinses, do After dry, as described class Graphene sample.Electrical conductivity 370s/cm of plant base class Graphene, specific surface area 760m2/ g, thickness 1-3nm.
Embodiment 4
(1) plant liquefaction: the bamboo scraps of drying and phenol are liquefied, obtains bio oil through filtering off except inorganic impurity.
(2) bio oil is mixed with catalyst: with nickel nitrate as catalyst, carries out according to mass ratio 0.7 1.0 with bio oil Mixing.
(3) seal pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is reactor volume 1/3, carry out airtight pretreatment.
(4) calcine: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, is warming up to 1200 with certain heating rate DEG C, keep 10h.After calcining terminates, natural cooling, takes out sample, reclaims catalyst through pickling, deionized water rinses, do After dry, as described class Graphene sample.Electrical conductivity 365s/cm of plant base class Graphene, specific surface area 730m2/ g, thickness 1-3nm.
Embodiment 5
(1) plant liquefaction: the bamboo scraps of drying and phenol are liquefied, obtains bio oil through filtering off except inorganic impurity.
(2) bio oil is mixed with catalyst: with iron series element nitrate as catalyst, with bio oil according to mass ratio 1.0 0.7 is mixed.
(3) seal pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is reactor volume 1/3, carry out airtight pretreatment.
(4) calcine: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, is warming up to 1200 with certain heating rate DEG C, keep 5h.After calcining terminates, natural cooling, takes out sample, reclaims catalyst through pickling, deionized water rinses, be dried Afterwards, as described class Graphene sample.Electrical conductivity 355s/cm of plant base class Graphene, specific surface area 718m2/ g, thickness 1- 3nm.
Embodiment 6
Bamboo scraps in embodiment 3 are changed to cedar sawdust, remaining, with embodiment 3, obtains the electrical conductivity of plant base class Graphene 369s/cm, specific surface area 751m2/ g, thickness 1-3nm.
Embodiment 7
Bamboo scraps raw material in embodiment 3 is changed to coconut husk, remaining, with embodiment 3, obtains the conductance of plant base class Graphene Rate 325s/cm, specific surface area 728m2/ g, thickness 1-3nm.
Embodiment 8
Nickel nitrate in embodiment 3 is changed to ferric nitrate, remaining, with embodiment 3, obtains the conductance of plant base class Graphene Rate 285s/cm, specific surface area 672m2/ g, thickness 1-3nm.
Embodiment 9
Nickel nitrate in embodiment 3 is changed to cobalt nitrate, remaining, with embodiment 3, obtains the conductance of plant base class Graphene Rate 370s/cm, specific surface area 760m2/ g, thickness 1-3nm.

Claims (6)

1. the preparation method of plant base class Graphene is it is characterised in that comprise the steps:
The first step, plant is liquefied: agricultural-forestry biomass raw material and the phenol of drying is liquefied, filters and obtain after removing inorganic impurity To bio oil;
Second step, bio oil is mixed with catalyst: with iron series element nitrate as catalyst, catalyst and bio oil are according to quality Mixed than (0.1~1.0) 1.0;
3rd step, seals pretreatment: a certain amount of said mixture is placed in spontaneous pressure reactor, inventory is less than reactor The 1/3 of volume, carries out airtight pretreatment;
4th step, calcining: the spontaneous pressure reactor that will be equipped with material is placed in high temperature furnace, heat up calcining, after calcining terminates, from So cool down, take out sample, reclaim catalyst through pickling, deionized water rinses, after being dried, as described plant base class Graphene Sample, electrical conductivity 370s/cm of plant base class Graphene, specific surface area 760m2/ g, thickness 1-3nm;Calcining heat be 500~ 1200 DEG C, calcination time 1-10h.
2. the preparation method of plant base class Graphene as claimed in claim 1 is it is characterised in that the plant described in the first step is former Material includes wood flour, bamboo scraps, straw, dries and uses.
3. the preparation method of plant base class Graphene as claimed in claim 1 is it is characterised in that bio oil described in the first step Remove solid impurity through filtering off.
4. the preparation method of plant base class Graphene as claimed in claim 1 is it is characterised in that iron series element bag in second step Include ferrum, nickel, cobalt.
5. the preparation method of plant base class Graphene as claimed in claim 1 is it is characterised in that iron series element nitre in second step At the uniform velocity stirred when hydrochlorate is mixed with bio oil.
6. the preparation method of the arbitrary described plant base class Graphene of claim 1 ~ 5 obtains Graphene is it is characterised in that conductance Rate 180~370s/cm, specific surface area 420~760m2/ g, thickness 1-3nm.
CN201510275731.1A 2015-05-26 2015-05-26 Plant-based graphene and preparation method thereof Active CN104891479B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510275731.1A CN104891479B (en) 2015-05-26 2015-05-26 Plant-based graphene and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510275731.1A CN104891479B (en) 2015-05-26 2015-05-26 Plant-based graphene and preparation method thereof

Publications (2)

Publication Number Publication Date
CN104891479A CN104891479A (en) 2015-09-09
CN104891479B true CN104891479B (en) 2017-02-01

Family

ID=54024519

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510275731.1A Active CN104891479B (en) 2015-05-26 2015-05-26 Plant-based graphene and preparation method thereof

Country Status (1)

Country Link
CN (1) CN104891479B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017063434A1 (en) * 2015-10-15 2017-04-20 济南圣泉集团股份有限公司 Carbon-containing nanostructure composite, polymer material using same and preparation method
CN105525377B (en) 2015-11-26 2018-08-17 济南圣泉集团股份有限公司 A kind of functional regenerated cellulose fibre and its preparation method and application
JP6853249B2 (en) 2015-11-20 2021-03-31 済南聖泉集団股▲ふん▼有限公司Jinan Shengquan Group Share Holding Co., Ltd Modified latex containing graphene and its preparation method and use
CN106082195A (en) * 2016-06-17 2016-11-09 青岛大学 A kind of ball milling formula preparation method of Graphene
CN106882799B (en) * 2017-03-04 2020-07-31 桂林理工大学 Sisal fiber-based nitrogen and sulfur co-doped graphene carbon material and preparation method thereof
CN110240147B (en) * 2019-05-30 2021-03-26 华中科技大学 Device for preparing graphene by using biomass pyrolysis oil
CN113023705A (en) * 2021-02-05 2021-06-25 江苏大学 Preparation method of hydrogen-rich carbon material and application of hydrogen-rich carbon material in lithium-sodium-potassium energy storage
US20240059952A1 (en) * 2022-08-22 2024-02-22 Halliburton Energy Services, Inc. Graphene Fluid Utilized to Suspend Particulates
US20240059608A1 (en) * 2022-08-22 2024-02-22 Halliburton Energy Services, Inc. Use of Graphene to Enhance Stability and Density Control of Cement Slurries
CN116654912A (en) * 2023-05-30 2023-08-29 吉林省格瑞节能科技有限公司 Preparation method and application of rice hull-based porous graphene

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101830460A (en) * 2010-05-26 2010-09-15 中国科学技术大学苏州研究院 Active carbon particles and preparation method thereof
CN102107864A (en) * 2009-12-24 2011-06-29 华北电力大学 Method for preparing biomass conductive carbon
CN102153067A (en) * 2010-12-16 2011-08-17 中国林业科学研究院木材工业研究所 Method for preparing high-conductivity wood conductive carbon powder by catalyzing metal oxide
CN102502598A (en) * 2011-10-25 2012-06-20 合肥工业大学 Catalytic graphitization method for wood powder
CN102807211A (en) * 2012-08-24 2012-12-05 北京化工大学 Graphene spherical assembly and preparation method thereof
CN103193223A (en) * 2013-04-02 2013-07-10 中国矿业大学 Controllable synthetic method of graphitized carbon spheres with hollow structure
TW201427898A (en) * 2013-01-15 2014-07-16 Micc Tec Co Ltd Method for fabricating reduced graphene oxide
CN104016341A (en) * 2014-07-01 2014-09-03 济南圣泉集团股份有限公司 Preparation method of porous graphene
CN104118873A (en) * 2014-08-13 2014-10-29 济南圣泉集团股份有限公司 Method for preparing active porous graphene

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102107864A (en) * 2009-12-24 2011-06-29 华北电力大学 Method for preparing biomass conductive carbon
CN101830460A (en) * 2010-05-26 2010-09-15 中国科学技术大学苏州研究院 Active carbon particles and preparation method thereof
CN102153067A (en) * 2010-12-16 2011-08-17 中国林业科学研究院木材工业研究所 Method for preparing high-conductivity wood conductive carbon powder by catalyzing metal oxide
CN102502598A (en) * 2011-10-25 2012-06-20 合肥工业大学 Catalytic graphitization method for wood powder
CN102807211A (en) * 2012-08-24 2012-12-05 北京化工大学 Graphene spherical assembly and preparation method thereof
TW201427898A (en) * 2013-01-15 2014-07-16 Micc Tec Co Ltd Method for fabricating reduced graphene oxide
CN103193223A (en) * 2013-04-02 2013-07-10 中国矿业大学 Controllable synthetic method of graphitized carbon spheres with hollow structure
CN104016341A (en) * 2014-07-01 2014-09-03 济南圣泉集团股份有限公司 Preparation method of porous graphene
CN104118873A (en) * 2014-08-13 2014-10-29 济南圣泉集团股份有限公司 Method for preparing active porous graphene

Also Published As

Publication number Publication date
CN104891479A (en) 2015-09-09

Similar Documents

Publication Publication Date Title
CN104891479B (en) Plant-based graphene and preparation method thereof
EP3266743B1 (en) Method for preparing biomass graphene by using cellulose as raw material
Feng et al. Ultrasonic assisted etching and delaminating of Ti3C2 Mxene
CN102464313B (en) Preparation method of graphene
CN102757036B (en) Preparation method of porous graphene
Xie et al. Efficient electromagnetic wave absorption performances dominated by exchanged resonance of lightweight PC/Fe3O4@ PDA hybrid nanocomposite
CN106587017A (en) Porous graphene and preparation method thereof
CN105271170B (en) Preparation method of nano carbon and composite material of nano carbon
CN102583324B (en) Preparation method of amorphous state carbon nano tube
CN103407991B (en) Preparation method of nickel/nickel oxide-decorated nitrogen-doped graphene material
Xiao et al. Porous carbon derived from rice husks as sustainable bioresources: Insights into the role of micro/mesoporous hierarchy in Co3O4/C composite for asymmetric supercapacitors
CN102583338A (en) High-quality graphene powder and preparation method thereof
CN102718250A (en) Method for preparing carbon-material-carrying tin dioxide nanosheet composite material
CN104386676B (en) A kind of preparation method of graphene
CN102464312B (en) Preparation method of graphene
CN102757035B (en) Preparation method of graphene
CN107393622B (en) Graphene-titanium suboxide composite conductive agent and preparation method thereof
Elanthamilan et al. Effective conversion of Cassia fistula dry fruits biomass into porous activated carbon for supercapacitors
CN103951916A (en) RGO (Reduced Graphene oxide)/ferric oxide-filled polyvinylidene fluoride composite wave-absorbing material and preparation method thereof
CN112093801B (en) Rice hull-based nano silicon carbide/carbon composite wave-absorbing material and preparation method thereof
CN106082194B (en) A kind of method for preparing bigger serface and the less graphene of the number of plies
CN107161989A (en) A kind of preparation method of cellular three-dimensional grapheme
CN106976854A (en) A kind of method for preparing carbon material
CN108940327B (en) Preparation method of sulfur-carbon-based solid acid catalyst
CN103316711A (en) Preparation method of graphene-like carbon nitride photocatalytic material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant