CN110182799A - It is a kind of to manufacture nitrogenous active carbon and its manufacturing method with anthracite - Google Patents
It is a kind of to manufacture nitrogenous active carbon and its manufacturing method with anthracite Download PDFInfo
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- CN110182799A CN110182799A CN201910525683.5A CN201910525683A CN110182799A CN 110182799 A CN110182799 A CN 110182799A CN 201910525683 A CN201910525683 A CN 201910525683A CN 110182799 A CN110182799 A CN 110182799A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/318—Preparation characterised by the starting materials
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/336—Preparation characterised by gaseous activating agents
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
Nitrogenous active carbon and its manufacturing method are manufactured with anthracite the invention discloses a kind of, it is characterized in that without powder processed, molding procedure in the Activated Carbon Production, anthracite is broken into certain particle size particle, it is added to be activated in activation furnace by high-temperature water vapor method and active carbon is made, nitrogen or inert gas purge quartz ampoule and sample are passed through to active carbon, it is then passed through nitrogen source in quartz ampoule, then carries out carbonization treatment and be activated to obtain nitrogenous active carbon;Above-mentioned nitrogenous active carbon is sufficiently washed with dilute hydrochloric acid, then is repeatedly washed with water, product is finally dried to obtain.The present invention has the advantage that 1. greatly shorten, simplify process route, reduce investment of founding the factory, save the energy, low production cost.2. avoiding the environmental pollution in production due to eliminating coal dust process processed;3. avoiding the pollution of product itself resulting from due to being added without the substances such as coal tar, pitch in production process of activated carbon, the application range of active carbon is expanded.
Description
Technical field
The invention belongs in chemical products charcoal and its compound field, in particular to it is a kind of manufactured with anthracite it is nitrogenous
Active carbon and its manufacturing method.
Background technique
It is each that the active carbon adsorbent excellent as one kind is widely used in each row such as chemical industry, food, medicine, environmental protection
Industry.It is increasing to the demand of active carbon both at home and abroad with world industry development and the deep progress to enviromental protection and improvement.
The country manufactures nitrogenous active carbon with anthracite at present, the process generallyd use are as follows:
1. coal dust is made in anthracite;
2. by coal dust, coal tar (binder), the stirring of a small amount of water, mediating, glazing beads molding;
3. molding mass is carbonized;
4. Slapple activating furnace is added in carbonized material, activated using high-temperature water vapor activation method;
5. the active carbon after activation is crushed, it is sieved into nitrogenous active carbon.
" by the method for coal manufacture granular active carbon " (publication number GK87100558) as disclosed in Patent Office of the People's Republic of China 87 years,
The main points of this method are: taking 10 parts of weight coal dusts to add 4.5-8 parts of heat adhesives and appropriate hot water is added to mix and stir molding, mix and stir and contain in material
3.6-5.2 parts of asphalitine, material after molding bakes hard processing 1-4 hours at 200-440 DEG C, then carbonizes at 450-600 DEG C
Processing then carries out pickling processes to iron-content and is lower than 0.2%, is activated after washing, drying.
The above-mentioned method with anthracite production active carbon has the following problems:
1. production technology is complicated, manufacture product process spends the time long;
2. large scale equipment needed for producing is more, investment is big;
3. contamination phenomenon is serious in production process, coal dust process contamination production environment such as processed, and unfavorable to producer's health.
Coal tar, pitch etc. is added to pollute active carbon itself, applies activated carbon product by limitation (as eaten
Product, medical and health industry cannot use, and the processing of drinking water is restricted).
Summary of the invention
The purpose of the present invention is the shortcomings for existing product and production technology, provide a kind of manufactured with anthracite and contain
The active carbon and its manufacturing method of nitrogen.
The technical solution of the present invention is as follows: using anthracite for raw material, without powder processed, molding procedure, anthracite is broken into
Grain particles (particle size range 1-8mm) required by product pass through high-temperature water vapor (temperature 850-980 in activation furnace
DEG C) activated obtained activated carbon product.Activation section of the raw material in furnace is 50-80 hours by the time.It is obtained nitrogenous
Active carbon can reach following technical indicator: iodine sorption value 800-1100mg/g, Penetrating curve 50-80%, and serge blue takes off
Color power 120-220mg/g, intensity 90-100%, as water purification charcoal without floating.
The present invention has the advantage that
1. greatly shortening, simplifying process route, reduce investment of founding the factory, save the energy, low production cost.
2. avoiding the environmental pollution in production due to eliminating coal dust process processed;
3. avoiding product resulting from due to being added without the substances such as coal tar, pitch in production process of activated carbon
The pollution of itself expands the application range of active carbon.
Specific embodiment
The embodiment of the present invention is as follows:
Embodiment one: Tai Xi smokeless fine purifiation coal in Ningxia is crushed, particle size range 2-5mm is sieved into, is directly added into Si Liepu
In activation furnace, it is 850-980 DEG C by high-temperature water vapor, activation temperature, passes through the activation section time about 50 hours.It is logical to active carbon
Enter nitrogen or inert gas purge quartz ampoule and sample, nitrogen source is then passed through in quartz ampoule, then carries out carbonization treatment and work
Change handles to obtain nitrogenous active carbon;Above-mentioned nitrogenous active carbon is sufficiently washed with dilute hydrochloric acid, then is repeatedly washed with water, finally
It is dried to obtain product.
Wherein, the nitrogen source is ammonia, magnesium nitride at least one;The talk processing includes: to be lived with microwave irradiation
Change processing, microwave irradiation power are 400-1200W, and the time of microwave irradiation is 6-20 minutes.
The activation processing carries out simultaneously with carbonization treatment, and carburizing temperature is 500-1200 DEG C.
For the nitrogenous active carbon using the salt acid elution that concentration is that 1.8-2.6mol/ rises, wash time is that 10-20 is small
When, wash temperature is 60-80 DEG C, then is repeatedly washed with water, and the drying temperature after washing is 70-120 DEG C, and drying time is greater than 10
Hour.
Iodine sorption value > 900mg/g, four chlorination charcoal > 55%, serge blue decolorizing ability > 120m g/g, intensity can be produced
The nitrogenous active carbon of > 95%.
Embodiment two: by the smokeless fine purifiation coal crushing and screening of Ningxia Tai Xi at particle size range 1-3mm, it is added directly into Si Liepu
In activation furnace, by high-temperature water vapor, 850-980 DEG C of activation temperature, pass through activation section time about 70 hours in furnace.To active carbon
Be passed through nitrogen or inert gas purge quartz ampoule and sample, nitrogen source be then passed through in quartz ampoule, then carry out carbonization treatment and
Activation processing obtains nitrogenous active carbon;Above-mentioned nitrogenous active carbon is sufficiently washed with dilute hydrochloric acid, then is repeatedly washed with water, most
After be dried to obtain product.
Wherein, the nitrogen source is ammonia, magnesium nitride at least one;The talk processing includes: to be lived with microwave irradiation
Change processing, microwave irradiation power are 400-1200W, and the time of microwave irradiation is 6-20 minutes.
The activation processing carries out simultaneously with carbonization treatment, and carburizing temperature is 500-1200 DEG C.
For the nitrogenous active carbon using the salt acid elution that concentration is that 1.8-2.6mol/ rises, wash time is that 10-20 is small
When, wash temperature is 60-80 DEG C, then is repeatedly washed with water, and the drying temperature after washing is 70-120 DEG C, and drying time is greater than 10
Hour.
The present embodiment can produce iodine sorption value > 900mg/g, four chlorination charcoal > 55%, serge blue decolorizing ability > 120m
The nitrogenous active carbon of g/g, intensity > 95%.
Embodiment three: by (950 DEG C of temperature >) after the smokeless fine purifiation coal calcination of Ningxia Tai Xi, crushing and screening is at particle size range 1-
3mm is directly added into Slapple activating furnace, 850-980 DEG C of activation temperature, small by activation section about 60 by high-temperature water vapor
When.It is passed through nitrogen or inert gas purge quartz ampoule and sample to active carbon, nitrogen source is then passed through in quartz ampoule, is then carried out
Carbonization treatment and activation processing obtain nitrogenous active carbon;Above-mentioned nitrogenous active carbon is sufficiently washed with dilute hydrochloric acid, then uses water
Repeatedly washing, is finally dried to obtain product.
Wherein, the nitrogen source is ammonia, magnesium nitride at least one;The talk processing includes: to be lived with microwave irradiation
Change processing, microwave irradiation power are 400-1200W, and the time of microwave irradiation is 6-20 minutes.
The activation processing carries out simultaneously with carbonization treatment, and carburizing temperature is 500-1200 DEG C.
For the nitrogenous active carbon using the salt acid elution that concentration is that 1.8-2.6mol/ rises, wash time is that 10-20 is small
When, wash temperature is 60-80 DEG C, then is repeatedly washed with water, and the drying temperature after washing is 70-120 DEG C, and drying time is greater than 10
Hour.
The present embodiment can produce iodine number > 950mg/g, carbon tetrachloride > 60%, serge blue decolorizing ability > 160mg/g, strong
Spend the nitrogenous active carbon of > 95%.
Example IV: Tai Xi smokeless fine purifiation coal in Ningxia being crushed, 1-3mm is sieved into, (the temperature 500-800 after carbonizing
DEG C), it is added in Slapple activating furnace, it is small by the activation section time about 50 by 850-980 DEG C of high-temperature water vapor, activation temperature
When.It is passed through nitrogen or inert gas purge quartz ampoule and sample to active carbon, nitrogen source is then passed through in quartz ampoule, is then carried out
Carbonization treatment and activation processing obtain nitrogenous active carbon;Above-mentioned nitrogenous active carbon is sufficiently washed with dilute hydrochloric acid, then uses water
Repeatedly washing, is finally dried to obtain product.
Wherein, the nitrogen source is ammonia, magnesium nitride at least one;The talk processing includes: to be lived with microwave irradiation
Change processing, microwave irradiation power are 400-1200W, and the time of microwave irradiation is 6-20 minutes.
The activation processing carries out simultaneously with carbonization treatment, and carburizing temperature is 500-1200 DEG C.
For the nitrogenous active carbon using the salt acid elution that concentration is that 1.8-2.6mol/ rises, wash time is that 10-20 is small
When, wash temperature is 60-80 DEG C, then is repeatedly washed with water, and the drying temperature after washing is 70-120 DEG C, and drying time is greater than 10
Hour.
The present embodiment can produce iodine > 950mg/g, Penetrating curve > 60%, serge blue decolorizing ability > 160mg/
G, the nitrogenous active carbon of intensity > 95%.
Claims (10)
1. a kind of manufacture nitrogenous active carbon and its manufacturing method with anthracite, it is characterised in that without system in the Activated Carbon Production
Anthracite is broken into certain particle size particle, is added in activation furnace and is activated system by high-temperature water vapor method by powder, molding procedure
Active carbon is obtained, nitrogen or inert gas purge quartz ampoule and sample is passed through to active carbon, nitrogen source is then passed through in quartz ampoule, so
It carries out carbonization treatment afterwards and is activated to obtain nitrogenous active carbon;Above-mentioned nitrogenous active carbon is sufficiently washed with dilute hydrochloric acid,
It is repeatedly washed with water again, is finally dried to obtain product.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 2. according to claim 1, it is characterised in that
The anthracite for being broken into certain particle size particle is added directly into activation furnace, activity is made by high-temperature water vapor activation method
Charcoal.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 3. according to claim 1, it is characterised in that
By the anthracite for being broken into certain particle size particle after charing (500-800 DEG C of temperature), it is added in activation furnace, passes through high temperature
Steam activation legal system obtains active carbon.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 4. according to claim 1, it is characterised in that
By (950 DEG C of temperature >) after calcined anthracite, it is broken into certain particle size particle, is then added in activation furnace, is steamed by high-temperature water
Active carbon is made in vapour activation method.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 5. according to claim 1, it is characterised in that
The raw material in activation furnace is added at 850-980 DEG C, is 50-80 hours by the activation section time.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 6. according to claim 1, it is characterised in that
Into activation furnace raw material granularity range between 1-8mm.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 7. according to claim 1, it is characterised in that
Activated carbon product index can reach: iodine sorption value 800-1100mg/g, Penetrating curve 50-80%, serge blue decolorizing ability
120-220mg/g, intensity 90-100%, as water purification charcoal without floating.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 8. according to claim 1, it is characterised in that
The nitrogen source is ammonia, magnesium nitride at least one;The talk processing includes: to be activated with microwave irradiation, microwave spoke
It is 400-1200W according to power, the time of microwave irradiation is 6-20 minutes.
A kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite 9. according to claim 1, it is characterised in that:
The activation processing carries out simultaneously with carbonization treatment, and carburizing temperature is 500-1200 DEG C.
10. it is according to claim 1 it is a kind of nitrogenous active carbon and its manufacturing method are manufactured with anthracite, feature exists
In: the nitrogenous active carbon is using the salt acid elution that concentration is that 1.8-2.6mol/ rises, and wash time is 10-20 hours, washing
Temperature is 60-80 DEG C, then is repeatedly washed with water, and the drying temperature after washing is 70-120 DEG C, and drying time is greater than 10 hours.
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01242409A (en) * | 1988-03-24 | 1989-09-27 | Osaka Gas Co Ltd | Production of activated carbon |
CN1194235A (en) * | 1997-06-25 | 1998-09-30 | 宁夏万得吸附技术研究所 | Amorphous particulate active carbon made from antiracite and its producing method |
CN103265029A (en) * | 2013-05-02 | 2013-08-28 | 石河子大学 | Mesoporous coal-based active carbon and microwave heating oriented preparation method thereof |
CN104445194A (en) * | 2014-12-04 | 2015-03-25 | 大连理工大学 | Mild and simple method for preparing heteroatom-doped coal-based activated carbon material |
CN107555433A (en) * | 2017-10-26 | 2018-01-09 | 电子科技大学 | Anthracite nitrating activated carbon and preparation method thereof |
CN109678151A (en) * | 2019-01-24 | 2019-04-26 | 中国矿业大学 | A kind of preparation method and application of anthracite-base nitrogen-doped porous carbon material |
CN109678153A (en) * | 2019-01-24 | 2019-04-26 | 中国矿业大学 | The preparation method and its catalytic applications in fuel battery negative pole of a kind of N doping porous carbon |
-
2019
- 2019-06-18 CN CN201910525683.5A patent/CN110182799A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01242409A (en) * | 1988-03-24 | 1989-09-27 | Osaka Gas Co Ltd | Production of activated carbon |
CN1194235A (en) * | 1997-06-25 | 1998-09-30 | 宁夏万得吸附技术研究所 | Amorphous particulate active carbon made from antiracite and its producing method |
CN103265029A (en) * | 2013-05-02 | 2013-08-28 | 石河子大学 | Mesoporous coal-based active carbon and microwave heating oriented preparation method thereof |
CN104445194A (en) * | 2014-12-04 | 2015-03-25 | 大连理工大学 | Mild and simple method for preparing heteroatom-doped coal-based activated carbon material |
CN107555433A (en) * | 2017-10-26 | 2018-01-09 | 电子科技大学 | Anthracite nitrating activated carbon and preparation method thereof |
CN109678151A (en) * | 2019-01-24 | 2019-04-26 | 中国矿业大学 | A kind of preparation method and application of anthracite-base nitrogen-doped porous carbon material |
CN109678153A (en) * | 2019-01-24 | 2019-04-26 | 中国矿业大学 | The preparation method and its catalytic applications in fuel battery negative pole of a kind of N doping porous carbon |
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Application publication date: 20190830 |