CN110526240A - A kind of method of purification of natural micro crystal graphite - Google Patents

A kind of method of purification of natural micro crystal graphite Download PDF

Info

Publication number
CN110526240A
CN110526240A CN201910866211.6A CN201910866211A CN110526240A CN 110526240 A CN110526240 A CN 110526240A CN 201910866211 A CN201910866211 A CN 201910866211A CN 110526240 A CN110526240 A CN 110526240A
Authority
CN
China
Prior art keywords
graphite
micro crystal
purification
crystal graphite
solution
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.)
Pending
Application number
CN201910866211.6A
Other languages
Chinese (zh)
Inventor
毋伟
席国强
王武
郭丙炎
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.)
Beijing University of Chemical Technology
Original Assignee
Beijing University of Chemical Technology
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 Beijing University of Chemical Technology filed Critical Beijing University of Chemical Technology
Priority to CN201910866211.6A priority Critical patent/CN110526240A/en
Publication of CN110526240A publication Critical patent/CN110526240A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/15Nano-sized carbon materials
    • C01B32/182Graphene
    • C01B32/194After-treatment
    • C01B32/196Purification

Abstract

A kind of method of purification of natural micro crystal graphite, belongs to technical field of graphite purification.Method includes the following steps: step 1, using natural micro crystal graphite as raw material, it is reacted with being sufficiently stirred under the alternative current of 2~16V after the NaOH solution mixing that molar concentration is 1M~8M, alternating frequency is 0.01~0.1Hz, then separates solution with graphite, washs, drying and obtain alkali cleaning graphite;Step 2, using alkali cleaning graphite as raw material, by the H of alkali cleaning graphite and 1~10M2SO4It is added in water heating kettle together, the impregnation under high-temperature pressurizing, solution and graphite centrifugation, suction filtration is obtained into pickling graphite after reaction;Step 3, pickling graphite is dried at high temperature, and removes volatile matter, obtain micro crystal graphite of the carbon content 99% or more.This method reaction condition is mild, and low energy consumption, and environmental pollution is small, and waste liquid is easy to handle, does not destroy graphite-structure, and purification efficiency is high.

Description

A kind of method of purification of natural micro crystal graphite
Technical field
The present invention relates to a kind of methods of purification of natural graphite, and natural micro crystal graphite especially lesser to partial size mentions The method that pure and mild condition, environmental pollution are small, purification efficiency is high.
Background technique
Graphite is a kind of high energy crystal carbon material, because of its unique structure and high temperature resistant, thermally conductive, lubrication, thermal shock resistance, change Learn the superperformances such as stability is good, be widely used in metallurgy, machinery, chemical industry, fire resisting, new energy, electronics, medicine, military project and The fields such as aerospace.
There is a large amount of natural graphite mineral, including crystalline flake graphite and micro crystal graphite (MG) on earth.The latter usually has < 1 μm of small crystalline size and carbon content is higher.China is the existing explored maximum micro crystal graphite storage site in Asia or even the world, lake The largest domestic mine reserve in southern province Chenzhou City reed pool area is more than 30,000,000 tons.In addition, the Inner Mongol (Bayan nguktrum), Hubei Also there are other main mineral deposits in (Shiyan), Fujian (Sanming City), the provinces such as Jilin (huge rock) and Heilungkiang (Yichuan).Some Mineral Deposits of Europe Grade is about 55%, and the grade in China Partial micro crystal graphite mineral deposit is 50%-85%.
There are two Main Trends of The Development for natural microcrystalline graphite product in modern industry, and one is high-purity, the other is super Fine grained.But micro crystal graphite crystal grain is tiny, partial impurities (quartz, silicate mineral, aluminium oxide, magnesium, calcium and other non-graphite groups Point) be wrapped in inside crystal grain aggregate and be difficult to separate, lead to purify that difficulty is big, this is to restrict micro crystal graphite in high-technology field Using and development an important factor for one of.
Micro crystal graphite purifying method common at present includes floatation, hydrogen fluoride, hydrofluoric acid-hydrochloric acid (sulfuric acid) nitration mixture Method, high temperature method, chlorinating roasting, alkali acid system etc..But these methods suffer from respective disadvantage in terms of industrial application.
He Guoshuai etc. (He Guoshuai, Hunan Lu Tang cryptocrystalline graphite mine Experimental study on ore dressing, mineral products protection and utilization, 2018,5, 57-61) selecting kerosene is collecting agent, and sodium carbonate is dispersing agent, using sec-octyl alcohol as foaming agent, is consolidated micro crystal graphite using floatation Determine carbon content and is promoted to 87.26% from 70.28%.(Jiang Fang, hydrochloric acid-hydrofluoric acid purifying prepare micro crystal graphite research, carbon to Jiang Fang etc. Plain technology, 2014,5,23-25) using HC1-HF mixed acid process purification micro crystal graphite, have studied the concentration and reaction of HC1 and HF Fixed carbon content is increased to 99.36% by influence of the time to refining effect.But since hydrofluoric acid toxicity is big, corrosivity is strong, right Human body and environmental hazard are larger, this constrains the application of this method significantly.Wen Zhonghua (application number: 201310128084.2) etc. logical Design high temperature method continuous industrial graphite purification furnace body is crossed, high-purity micro crystal graphite of purity 99.99% is obtained.But the method exists The disadvantages of equipment is expensive, and energy consumption is high, working condition harshness and small yield, is only applicable to produce ultra-pure graphite.Chlorinating roasting Refining effect is good, at low cost, but the toxicity of chlorine and corrosivity can generate grave danger to human body and ecological environment, in addition, chlorine The process system for changing roasting method is unstable, and the grade of graphite concentrate fluctuates the factors such as larger and also affects the method to a certain extent Practical application.
It is to be mixed in a certain ratio graphite and NaOH solid that alkali acid system, which purifies graphite, is put into stove and is calcined, In NaOH is reacted under high temperature with molten condition and the metal oxide in graphite, mainly generates sodium metaaluminate or silicates Object is closed, its molten filters in water is removed, remaining unreacted metal oxide dissolves in acid condition, further increases production The purity of object.Although above-mentioned alkali acid system refining effect is good, wastewater treatment is relatively easy, and energy consumption is high, complex process, the reaction time It is long, and equipment seriously corroded, the micro crystal graphite grade after furthermore purifying still are difficult to reach the requirement of high purity graphite.(the ginger such as Jiang Fang Virtue, alkali acid system purify certain micro crystal graphite metal mine, 2014,32 (9): 82-84) tradition is used to Certain District, Hunan micro crystal graphite Alkali acid system is purified, by fixed carbon content be 85% graphite purification to 98.79%.
Summary of the invention
The purpose of the present invention is for existing alkali acid system purify natural micro crystal graphite there are the shortcomings that, on this basis into Row improves, and provides a kind of mild condition, environmental-friendly and high purification efficiency natural micro crystal graphite purifying method.
The technical scheme of the present invention is realized as follows:
A kind of method of purification of natural micro crystal graphite, which comprises the following steps:
Step 1, it using natural micro crystal graphite as raw material, is reacted under alternative current with after NaOH solution mixing, while sufficiently It is stirred to react solution, solution and graphite are centrifugated after reaction, washes, filter and obtain alkali cleaning graphite after drying;
Step 2, by alkali cleaning graphite and H2SO4It is added in water heating kettle after solution mixing, impregnation under high temperature, reaction knot Solution and graphite are centrifugated after beam, obtain pickling graphite after washing, filtering.
Step 3, volatile matter is being dried and removed to pickling graphite, the micro crystal graphite purified.
It is preferred that natural micro crystal graphite purity is 80%~90%, partial size is 1~10 μm.
It is preferred that mass concentration of the micro crystal graphite in NaOH solution is 0.2~0.4g/ml, the molar concentration of NaOH solution is 1~8M.
The voltage for replacing DC current applied in preferred steps 1 is 2~16V, and alternating frequency is 0.01~0.1Hz.
2~10h is stirred to react in preferred steps 1 under power on condition, reaction temperature is room temperature.
It is preferred that alkali cleaning micro crystal graphite is in H2SO4Mass concentration in solution are as follows: 0.2~0.5g/ml, H2SO4Molar concentration For 1~10M.
The time of 2 high temperature hydro-thermal impregnation of preferred steps is 2~16h, and reaction temperature is 100~180 DEG C.
It is first centrifuged in preferred steps 3 and separates pickling graphite with solution, suction filtration is then washed with water to cleaning solution pH value 6 ~7, volatile matter is dried and removed to gained filter cake, obtains the micro crystal graphite of high-purity.
Using method of purification of the invention, micro crystal graphite can be fixed carbon content from 80%~90% improve to 99% with On, and lost substantially without graphite in the process.Compared with the alkali acid system being widely used at present, by the present invention in that at electrochemistry Reason not only greatly reduces energy consumption, moreover it is possible to avoid the oxidation and matter of graphite at high temperature instead of the high-temperature fusion process of NaOH Amount loss.The advantages that this method has mild condition, and low energy consumption, environmental-friendly, and waste liquid is easy to handle.
Detailed description of the invention
Fig. 1 micro crystal graphite purification schemes schematic diagram;
1 micro crystal graphite of Fig. 2 embodiment purification front and back XRD analysis.
Specific embodiment
In order to make the object, technical scheme and advantages of the embodiment of the invention clearer, below in conjunction with the embodiment of the present invention, The technical solution of the embodiment of the present invention is clearly and completely described.Obviously, described embodiment is of the invention one Point embodiment, rather than limiting the scope of the present invention.
The mode for applying alternative current is that two electrode bars or two opposite electrode plates, electrode are put into reaction solution Stick or electrode plate are separately connected alternate DC voltage.
Embodiment 1
The natural micro crystal graphite of fixed carbon content 80% is dried into certain time in air dry oven and removes moisture removal, then is taken 20g graphite is mixed with the NaOH solution of 8M, liquor capacity 100ml, applies the alternating electricity for+16V that frequency is 0.1Hz at room temperature Stream, reaction time 10h are sufficiently stirred simultaneously.Solution and graphite are centrifugated after reaction, repeated centrifugation several times, and After wash, filter and dry, obtain alkali cleaning graphite.
Take 4g alkali cleaning graphite and the H of 10M2SO4Mixing, H2SO4Volume is 10ml, at 100 DEG C of temperature, reaction time 10h's High pressure acidleach is carried out under hydrothermal condition, is after reaction centrifugated solution and graphite, and repeated centrifugation several times, is then washed It filters to soluble impurity and completely removes;Again by gained filter cake high temperature drying 5h, the microlite that fixed carbon content is 97.68% is obtained Ink, yield 99.9%, essentially absolutely.
Embodiment 2
The natural micro crystal graphite of fixed carbon content 80% is dried into certain time in air dry oven and removes moisture removal, then is taken 30g graphite is mixed with the NaOH solution of 2M, liquor capacity 100ml, applies+4V the alternative current that frequency is 0.1Hz at room temperature, Reaction time 10h, is sufficiently stirred simultaneously.Solution and graphite are centrifugated after reaction, repeated centrifugation several times, then water It washes, filter and dry, obtain alkali cleaning graphite.
Take 5g alkali cleaning graphite and the H of 4M2SO4Mixing, H2SO4Volume is 20ml, at 180 DEG C of temperature, reaction time 16h's High pressure acidleach is carried out under hydrothermal condition, is after reaction centrifugated solution and graphite, and repeated centrifugation several times, is then washed It filters to soluble impurity and completely removes;Again by gained filter cake high temperature drying 5h, the microlite that fixed carbon content is 98.13% is obtained Ink, yield 99.9%, essentially absolutely.
Embodiment 3
The natural micro crystal graphite of fixed carbon content 85% is dried into certain time in air dry oven and removes moisture removal, then is taken 40g micro crystal graphite is mixed with the NaOH solution of 3M, liquor capacity 100ml, is applied+the 10V that frequency is 0.02Hz at room temperature and is handed over For electric current, reaction time 7h is sufficiently stirred simultaneously.Solution and graphite are centrifugated after reaction, repeated centrifugation several times, It then washes, filter and dry, obtain alkali cleaning graphite.
Take 10g alkali cleaning graphite and the H of 4M2SO4Mixing, H2SO4Volume is 50ml, at 160 DEG C of temperature, reaction time 14h's High pressure acidleach is carried out under hydrothermal condition, is after reaction centrifugated solution and graphite, and repeated centrifugation several times, is then washed It filters to soluble impurity and completely removes;Again by filter cake high temperature drying 5h, the microlite that fixed carbon content is 99.02% is obtained Ink, yield 99.9%, essentially absolutely.
Embodiment 4
The natural micro crystal graphite of fixed carbon content 85% is dried into certain time in air dry oven and removes moisture removal, then is taken 40g micro crystal graphite is mixed with the NaOH solution of 5M, liquor capacity 100ml, is applied+the 8V that frequency is 0.1Hz at room temperature and is replaced Electric current, reaction time 8h, is sufficiently stirred simultaneously.Solution and graphite are centrifugated after reaction, repeated centrifugation several times, It then washes, filter and dry, obtain alkali cleaning graphite.
Take 5g alkali cleaning graphite and the H of 6M2SO4Mixing, H2SO4Volume is 20ml, at 160 DEG C of temperature, the water of reaction time 5h High pressure acidleach is carried out under heat condition, is after reaction centrifugated solution and graphite, and repeated centrifugation several times, then take out by washing Filter to soluble impurity completely removes;Again by filter cake high temperature drying 5h, the micro crystal graphite that fixed carbon content is 98.78% is obtained, Yield is 99.9%, essentially absolutely.
Embodiment 5
The natural micro crystal graphite of fixed carbon content 90% is dried into certain time in air dry oven and removes moisture removal, then is taken 20g micro crystal graphite is mixed with the NaOH solution of 2M, liquor capacity 80ml, is applied+the 12V that frequency is 0.05Hz at room temperature and is replaced Electric current, reaction time 7h, is sufficiently stirred simultaneously.Solution and graphite are centrifugated after reaction, repeated centrifugation several times, and After wash, filter and dry, obtain alkali cleaning graphite.
Take 10g alkali cleaning graphite and the H of 4M2SO4Mixing, H2SO4Volume is 50ml, at 180 DEG C of temperature, reaction time 14h's High pressure acidleach is carried out under hydrothermal condition, is after reaction centrifugated solution and graphite, and repeated centrifugation several times, is then washed It filters to soluble impurity and completely removes;Again by filter cake high temperature drying 5h, the microlite that fixed carbon content is 99.15% is obtained Ink, yield 99.9%, essentially absolutely.
Embodiment 6
The natural micro crystal graphite of fixed carbon content 90% is dried into certain time in air dry oven and removes moisture removal, then is taken 30g graphite is mixed with the NaOH solution of 3M, liquor capacity 100ml, and it is alternately electric to apply the+10V that frequency is 0.03Hz at room temperature Stream, reaction time 7h are sufficiently stirred simultaneously.Solution and graphite are centrifugated after reaction, repeated centrifugation several times, then It washes, filter and dry, obtain alkali cleaning graphite.
Take 10g alkali cleaning graphite and the H of 3M2SO4Mixing, H2SO4Volume is 50ml, at 160 DEG C of temperature, reaction time 14h's High pressure acidleach is carried out under hydrothermal condition, is after reaction centrifugated solution and graphite, and repeated centrifugation several times, is then washed It filters to soluble impurity and completely removes;Again by gained filter cake high temperature drying 5h, the microlite that fixed carbon content is 99.25% is obtained Ink, yield 99.9%, essentially absolutely.
Examples detailed above of the invention is merely to detailed description examples of the invention, all to belong to skill of the invention The variation that art scheme is amplified out is still in protection scope of the present invention.

Claims (8)

1. a kind of method of purification of natural micro crystal graphite, which comprises the following steps:
Step 1, it using natural micro crystal graphite as raw material, reacts under alternative current with after NaOH solution mixing, is sufficiently stirred simultaneously Solution and graphite are centrifugated after reaction, wash, filter and obtain alkali cleaning graphite after drying by reaction solution;
Step 2, by alkali cleaning graphite and H2SO4It is added in water heating kettle after solution mixing, impregnation under high temperature, after reaction Solution and graphite are centrifugated, obtain pickling graphite after washing, filtering;
Step 3, volatile matter is being dried and removed to pickling graphite, the micro crystal graphite purified.
2. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that natural micro crystal graphite is pure Degree is 80%~90%, and partial size is 1~10 μm.
3. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that micro crystal graphite is in NaOH Mass concentration in solution is 0.2~0.4g/ml, and the molar concentration of NaOH solution is 1~8M.
4. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that applied in step 1 Alternately the voltage of DC current is 2~16V, and alternating frequency is 0.01~0.1Hz.
5. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that be powered item in step 1 2~10h is stirred to react under part, reaction temperature is room temperature.
6. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that alkali cleaning micro crystal graphite exists H2SO4Mass concentration in solution are as follows: 0.2~0.5g/ml, H2SO4Molar concentration be 1~10M.
7. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that step 2 high temperature water The time of hot submersion reaction is 2~16h, and reaction temperature is 100~180 DEG C.
8. a kind of method of purification of natural micro crystal graphite described in accordance with the claim 1, which is characterized in that be first centrifuged in step 3 Pickling graphite is separated with solution, suction filtration is then washed with water to cleaning solution pH value 6~7, gained filter cake is dried and removed Volatile matter obtains the micro crystal graphite of high-purity.
CN201910866211.6A 2019-09-09 2019-09-09 A kind of method of purification of natural micro crystal graphite Pending CN110526240A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910866211.6A CN110526240A (en) 2019-09-09 2019-09-09 A kind of method of purification of natural micro crystal graphite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910866211.6A CN110526240A (en) 2019-09-09 2019-09-09 A kind of method of purification of natural micro crystal graphite

Publications (1)

Publication Number Publication Date
CN110526240A true CN110526240A (en) 2019-12-03

Family

ID=68668490

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910866211.6A Pending CN110526240A (en) 2019-09-09 2019-09-09 A kind of method of purification of natural micro crystal graphite

Country Status (1)

Country Link
CN (1) CN110526240A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102195865B1 (en) * 2020-04-07 2020-12-28 한국지질자원연구원 Method for high purification of graphite
CN115611278A (en) * 2022-10-31 2023-01-17 中国科学院过程工程研究所 Graphite purification method and device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011159922A2 (en) * 2010-06-16 2011-12-22 The Research Foundation Of State University Of New York Graphene films and methods of making thereof
CN104098092A (en) * 2014-08-03 2014-10-15 北京矿冶研究总院 Method for purifying natural microcrystalline graphite
CN104909354A (en) * 2014-12-12 2015-09-16 黑龙江科技大学 Graphite purification method
CN107555426A (en) * 2017-10-31 2018-01-09 湖南国盛石墨科技有限公司 A kind of low energy consumption is prepared on a large scale high-purity micro crystal graphite technique and its high-purity micro crystal graphite

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011159922A2 (en) * 2010-06-16 2011-12-22 The Research Foundation Of State University Of New York Graphene films and methods of making thereof
CN104098092A (en) * 2014-08-03 2014-10-15 北京矿冶研究总院 Method for purifying natural microcrystalline graphite
CN104909354A (en) * 2014-12-12 2015-09-16 黑龙江科技大学 Graphite purification method
CN107555426A (en) * 2017-10-31 2018-01-09 湖南国盛石墨科技有限公司 A kind of low energy consumption is prepared on a large scale high-purity micro crystal graphite technique and its high-purity micro crystal graphite

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
X.J. LU: ""Preparation of high-purity and low-sulphur graphite from Woxna"", 《MINERALS ENGINEERING》 *
华中一: "《真空实验技术 第1版》", 31 July 1986, 上海科学技术出版社 *
姜芳 等: ""碱酸法提纯某微晶石墨"", 《金属矿山》 *
朱碧馨: ""石墨的氧化及剥离新技术研究"", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102195865B1 (en) * 2020-04-07 2020-12-28 한국지질자원연구원 Method for high purification of graphite
CN115611278A (en) * 2022-10-31 2023-01-17 中国科学院过程工程研究所 Graphite purification method and device
CN115611278B (en) * 2022-10-31 2024-03-22 中国科学院过程工程研究所 Graphite purification method and device

Similar Documents

Publication Publication Date Title
CN101973545B (en) Method for purifying high-purity graphite
CN104003382B (en) A kind of high purity graphite chemical purification continuous producing method
CN101704687B (en) Method for producing potassium sulphate by decomposing potassium feldspar at low temperature
CN102718234B (en) Method for extracting lithium carbonate from lepidolite
CN109930174A (en) The method that aluminium electrolyte takes off lithium purification and recycling lithium
CN102020299B (en) Method for producing industrial activated aluminum oxide from pulverized fuel ash
CN106517256A (en) Method for producing lithium hydroxide monohydrate from lithium carbonate
CN109485036B (en) Method for recovering and treating waste cathode carbon blocks of aluminum electrolytic cell
CN101920957A (en) Preparation method of high-purity graphite
CN110526240A (en) A kind of method of purification of natural micro crystal graphite
CN109167118A (en) The method of comprehensive utilization of ferric phosphate lithium cell electrode material
CN108946772A (en) A method of pure Lithium Carbonate is prepared by lithium ore
JP3240741U (en) System for comprehensive recovery of metal resources in fly ash by molten salt electrolysis
CN106745128A (en) A kind of method of aluminium lime-ash removal of impurities
CN105271231A (en) Preparation method for two-dimensional nano Ti3C2 sheet
CN102786096A (en) Iron oxide for lithium iron phosphate battery, and its preparation method
CN104150478B (en) A kind of green circulatory technique of being prepared activated carbon for super capacitors material by rice husk
CN115156253B (en) Resource treatment method for aluminum electrolysis overhaul slag
CN108862270A (en) A kind of method of purification of artificial graphite
CN102020300B (en) Method for producing metallurgical-grade aluminum oxide by coal ash
CN102020303B (en) Method for producing ultra-high purity aluminium sulfate from fly ash
CN103193238A (en) Method for producing superfine white carbon black, ferric hydroxide and aluminum oxide by using coal ash
CN101209844B (en) Technique for preparing high quality boric acid from salt lake type boron ore by one-step method
CN102275904A (en) Method of preparing high-purity graphite by using chemical liquid-phase method
CN103014334B (en) Method for replacement dissolution of bastnaesite (bastnasite)

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20191203