CN1436723A - Desulfurizing and denitrating active carbon and its production process - Google Patents

Desulfurizing and denitrating active carbon and its production process Download PDF

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Publication number
CN1436723A
CN1436723A CN02160182A CN02160182A CN1436723A CN 1436723 A CN1436723 A CN 1436723A CN 02160182 A CN02160182 A CN 02160182A CN 02160182 A CN02160182 A CN 02160182A CN 1436723 A CN1436723 A CN 1436723A
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China
Prior art keywords
coal
tar
gac
temperature
weight percent
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CN02160182A
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CN1200876C (en
Inventor
姜荣跃
李怀珠
李同川
庞惠生
苏荣生
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Shanxi Xinhua Chemical Industry Co Ltd
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SHANXI XINHUA CHEMICAL PLANT
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Priority to CNB021601828A priority Critical patent/CN1200876C/en
Publication of CN1436723A publication Critical patent/CN1436723A/en
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Abstract

The present invention is one kind of active carbon produced with coal directly and its production process. The technological scheme is that the desulfurizing and denitrating active carbon is produced with coal powder in 62-72 wt%, tar 25-35 wt% and water 3-5 wt%. The production process includes the following steps: preparing coal powder, compounding tar, producing coal paste, pelletizing, carbonization, activation and oxidation. The active carbon product has the advantages of great specific surface area, high desulfurizing and denitrating effect and capacity of being regenerated for many times.

Description

Desulphurization denitration gac and production method thereof
One, technical field:
The present invention relates to a kind of desulphurization denitration gac and production method thereof, it belongs to a kind of gac and production method of directly making with coal thereof.
Two, background technology:
The gac of desulphurization denitration use is at present all made with semicoke and binding agent.It produces the desulphurization denitration process of active carbon: the gac of semicoke is done chemical treatment, to increase the ability of surface devulcanization denitration.Though the gac that aforesaid method is produced can desulphurization denitration, this gac exists still that specific surface area is little, intensity is low, mesopore is undeveloped and shortcoming such as desulfurization off sulfide effect difference.
Three, summary of the invention:
The objective of the invention is to solve that existing gac exists that specific surface area is little, intensity is low, mesopore is undeveloped and technological difficulties such as desulfurization off sulfide effect difference and desulphurization denitration gac and the production method thereof that a kind of gac specific surface area is big, intensity is high, mesopore is flourishing and desulfurization off sulfide effect is good is provided.
In order to realize above-mentioned task, the technical solution used in the present invention is: this desulphurization denitration gac, and it is made by coal dust, tar and water, and its weight percent is:
Coal dust 62~72% tar 25~35% water 3~5%.
Above-mentioned coal dust is made by bituminous coal and coking coal, and its weight percent is:
Bituminous coal 60~80% coking coal 20~40%.
The making method of above-mentioned desulphurization denitration gac is: it comprises the following steps:
1), preparation coal dust: at first bituminous coal, coking coal are broken into coal cinder respectively, after then bituminous coal and coking coal being cooperated by described weight percent, grind to form 300~400 purpose coal dusts again less than 12mm;
2), preparation tar: earlier the tar temperature is adjusted to 50~85 ℃, then stirs, then tar is mixed with asphalt content and is 50~72% mixed tar;
3), make coal cream: coal dust, the tar for preparing and the water of preparation are made coal cream by stirring in the described weight percent adding mixing machine;
4), molding, granulating: the coal cream of making sent into make bar dress particle in the shaper that pressure is 8.0~16.0Mpa;
5), charing: it is that charing was come out of the stove in 1.5~3.0 hours in 300~800 ℃ the charring furnace that the particle of moulding is added temperature, makes carbonized material;
6), activation: it is that 700~910 ℃, pressure are in the activation furnace of 50~150Pa that the carbonized material made is added temperature, is that 840~1100 ℃ steam activation was come out of the stove in 2~3 hours with temperature, makes that composing lives expects;
7), oxidation: the tax that will make is lived and is expected to add in the oxidized still gac that oxygen level is 12~21% in stove, the energy desulphurization denitration was made in oxidation in 1.5~3.0 hours when furnace temperature was 340~510 ℃.
Because the present invention adopted technique scheme, therefore compare with background technology, have that the gac specific surface area is big, intensity is high, mesopore is flourishing, functional group is rich on the surface, desulfurization off sulfide effect is good and regeneration times more than etc. advantage.
Four, embodiment:
Embodiment 1:
Desulphurization denitration gac in the present embodiment, it is made by coal dust, tar and water, and its weight percent is:
Coal dust 70% tar 25% water 5%.
Above-mentioned coal dust is made by bituminous coal and coking coal, and its weight percent is:
Bituminous coal 60% coking coal 40%.
The making method of above-mentioned gac is: it comprises the following steps:
1), preparation coal dust: at first bituminous coal, coking coal are broken into coal cinder respectively, after then bituminous coal and coking coal being cooperated by above-mentioned weight percent, grind to form 300 purpose coal dusts again less than 12mm;
2), preparation tar: earlier the tar temperature is adjusted to 55 ℃, then stirs, then tar being mixed with asphalt content is that 50% mixed tar and the temperature that makes it remain on 55 ℃;
3), make coal cream: coal dust, the tar for preparing and the water of preparation are made coal cream by stirring in the above-mentioned weight percent adding mixing machine;
4), molding, granulating: the coal cream of making sent in the shaper that pressure is 10Mpa make strip particle;
5), charing: it is that carbonization temperature rises to 800 ℃ by 300 ℃ in 300 ℃ the charring furnace that the particle of moulding is added temperature in, and charing was come out of the stove in 3 hours, made carbonized material;
6), activation: it is that 700 ℃, pressure are in the activation furnace of 50Pa that the carbonized material made is added temperature, is that 840 ℃ steam activation was come out of the stove in 3 hours with temperature, makes that composing lives expects;
7), oxidation: the tax that will make is lived and is expected to add in the oxidized still gac that oxygen level is 16% in stove, the energy desulphurization denitration was made in oxidation in 2 hours when furnace temperature was 400 ℃.
Embodiment 2:
Desulphurization denitration gac in the present embodiment, it is made by coal dust, tar and water, and its weight percent is:
Coal dust 62% tar 35% water 3%.
Above-mentioned coal dust is made by bituminous coal and coking coal, and its weight percent is:
Bituminous coal 80% coking coal 20%.
The making method of above-mentioned gac is: it comprises the following steps:
1), preparation coal dust: at first bituminous coal, coking coal are broken into coal cinder respectively, after then bituminous coal and coking coal being cooperated by above-mentioned weight percent, grind to form 400 purpose coal dusts again less than 12mm;
2), preparation tar: earlier the tar temperature is adjusted to 50 ℃, then stirs, then tar being mixed with asphalt content is that 60% mixed tar and the temperature that makes it remain on 50 ℃;
3), make coal cream: coal dust, the tar for preparing and the water of preparation are made coal cream by stirring in the above-mentioned weight percent adding mixing machine;
4), molding, granulating: the coal cream of making sent in the shaper that pressure is 8.0Mpa make strip particle;
5), charing: it is that carbonization temperature rises to 800 ℃ by 300 ℃ in 300 ℃ the charring furnace that the particle of moulding is added temperature in, and charing was come out of the stove in 2 hours, made carbonized material;
6), activation: it is that 800 ℃, pressure are in the activation furnace of 100Pa that the carbonized material made is added temperature, is that 970 ℃ steam activation was come out of the stove in 2.5 hours with temperature, makes that composing lives expects;
7), oxidation: the tax that will make is lived and is expected to add in the oxidized still gac that oxygen level is 12% in stove, the energy desulphurization denitration was made in oxidation in 3.0 hours when furnace temperature was 340 ℃.
Embodiment 3:
Desulphurization denitration gac in the present embodiment, it is made by coal dust, tar and water, and its weight percent is:
Coal dust 72% tar 25% water 3%.
Above-mentioned coal dust is made by bituminous coal and coking coal, and its weight percent is:
Bituminous coal 70% coking coal 30%.
The making method of above-mentioned gac is: it comprises the following steps:
1), preparation coal dust: at first bituminous coal, coking coal are broken into coal cinder respectively, after then bituminous coal and coking coal being cooperated by above-mentioned weight percent, grind to form 350 purpose coal dusts again less than 12mm;
2), preparation tar: earlier the tar temperature is adjusted to 85 ℃, then stirs, then tar being mixed with asphalt content is that 72% mixed tar and the temperature that makes it remain on 85 ℃;
3), make coal cream: coal dust, the tar for preparing and the water of preparation are made coal cream by stirring in the above-mentioned weight percent adding mixing machine;
4), molding, granulating: the coal cream of making sent in the shaper that pressure is 16.0Mpa make strip particle;
5), charing: it is that carbonization temperature rises to 800 ℃ by 300 ℃ in 300 ℃ the charring furnace that the particle of moulding is added temperature in, and charing was come out of the stove in 1.5 hours, made carbonized material;
6), activation: it is that 910 ℃, pressure are in the activation furnace of 150Pa that the carbonized material made is added temperature, is that 1100 ℃ steam activation was come out of the stove in 2 hours with temperature, makes that composing lives expects;
7), oxidation: the tax that will make is lived and is expected to add in the oxidized still gac that oxygen level is 21% in stove, the energy desulphurization denitration was made in oxidation in 1.5 hours when furnace temperature was 510 ℃.
Embodiment 4:
Desulphurization denitration gac in the present embodiment, it is made by coal dust, tar and water, and its weight percent is:
Coal dust 67% tar 29% water 4%.
Above-mentioned coal dust is made by bituminous coal and coking coal, and its weight percent is:
Bituminous coal 65% coking coal 35%.
The making method of above-mentioned gac is: it comprises the following steps:
1), preparation coal dust: at first bituminous coal, coking coal are broken into coal cinder respectively, after then bituminous coal and coking coal being cooperated by above-mentioned weight percent, grind to form 360 purpose coal dusts again less than 12mm;
2), preparation tar: earlier the tar temperature is adjusted to 60 ℃, then stirs, then tar being mixed with asphalt content is that 65% mixed tar and the temperature that makes it remain on 60 ℃;
3), make coal cream: coal dust, the tar for preparing and the water of preparation are made coal cream by stirring in the above-mentioned weight percent adding mixing machine;
4), molding, granulating: the coal cream of making sent in the shaper that pressure is 14Mpa make strip particle;
5), charing: it is that carbonization temperature rises to 800 ℃ by 300 ℃ in 300 ℃ the charring furnace that the particle of moulding is added temperature in, and charing was come out of the stove in 2.5 hours, made carbonized material;
6), activation: it is that 820 ℃, pressure are in the activation furnace of 90Pa that the carbonized material made is added temperature, is that 1000 ℃ steam activation was come out of the stove in 2.3 hours with temperature, makes that composing lives expects;
7), oxidation: the tax that will make is lived and is expected to add in the oxidized still gac that oxygen level is 15% in stove, the energy desulphurization denitration was made in oxidation in 1.8 hours when furnace temperature was 420 ℃.

Claims (3)

1, a kind of desulphurization denitration gac, it is characterized in that: it is made by coal dust, tar and water, and its weight percent is:
Coal dust 62~72% tar 25~35% water 3~5%.
2, a kind of desulphurization denitration gac according to claim 1, it is characterized in that: described coal dust is made by bituminous coal and coking coal, and its weight percent is:
Bituminous coal 60~80% coking coal 20~40%.
3, the making method of the described desulphurization denitration gac of a kind of production claim 1, it is characterized in that: it comprises the following steps:
1), preparation coal dust: at first bituminous coal, coking coal are broken into coal cinder respectively, after then bituminous coal and coking coal being cooperated by described weight percent, grind to form 300~400 purpose coal dusts again less than 12mm;
2), preparation tar: earlier the tar temperature is adjusted to 50~85 ℃, then stirs, then tar is mixed with asphalt content and is 50~72% mixed tar;
3), make coal cream: coal dust, the tar for preparing and the water of preparation are made coal cream by stirring in the described weight percent adding mixing machine;
4), molding, granulating: the coal cream of making sent in the shaper that pressure is 8.0~16.0Mpa make strip particle;
5), charing: it is that charing was come out of the stove in 1.5~3.0 hours in 300~800 ℃ the charring furnace that the particle of moulding is added temperature, makes carbonized material;
6), activation: it is that 700~910 ℃, pressure are in the activation furnace of 50~150Pa that the carbonized material made is added temperature, is that 840~1100 ℃ steam activation was come out of the stove in 2~3 hours with temperature, makes that composing lives expects;
7), oxidation: the tax that will make is lived and is expected to add in the oxidized still gac that oxygen level is 12~21% in stove, the energy desulphurization denitration was made in oxidation in 1.5~3.0 hours when furnace temperature was 340~510 ℃.
CNB021601828A 2002-12-28 2002-12-28 Desulfurizing and denitrating active carbon and its production process Expired - Lifetime CN1200876C (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100408474C (en) * 2006-08-01 2008-08-06 长春惠工净化工业有限公司 Production method of desulfur denitrate dust collecting active coke
CN104383876A (en) * 2014-10-23 2015-03-04 山西新华化工有限责任公司 Preparation method of granular active carbon for sewage treatment
CN105858650A (en) * 2016-03-22 2016-08-17 黎城蓝天燃气开发有限公司 Method for manufacturing desulfurization denitration activated carbon by using waste activated carbon
CN108975324A (en) * 2018-08-23 2018-12-11 大同新成新材料股份有限公司 A kind of desulphurization denitration active carbon and preparation method thereof and device
CN109384228A (en) * 2018-11-08 2019-02-26 辽宁科技大学 A kind of desulphurization denitration active carbon and preparation method thereof
CN110917833A (en) * 2019-12-13 2020-03-27 西安润川环保科技有限公司 Novel flue gas denitration method
CN114044515A (en) * 2021-11-04 2022-02-15 中欣环保科技有限公司 Preparation method of desulfurization and denitrification activated carbon

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100408474C (en) * 2006-08-01 2008-08-06 长春惠工净化工业有限公司 Production method of desulfur denitrate dust collecting active coke
CN104383876A (en) * 2014-10-23 2015-03-04 山西新华化工有限责任公司 Preparation method of granular active carbon for sewage treatment
CN105858650A (en) * 2016-03-22 2016-08-17 黎城蓝天燃气开发有限公司 Method for manufacturing desulfurization denitration activated carbon by using waste activated carbon
CN105858650B (en) * 2016-03-22 2018-03-20 黎城蓝天燃气开发有限公司 Utilize the method for waste and old activated carbon manufacture desulphurization denitration activated carbon
CN108975324A (en) * 2018-08-23 2018-12-11 大同新成新材料股份有限公司 A kind of desulphurization denitration active carbon and preparation method thereof and device
CN109384228A (en) * 2018-11-08 2019-02-26 辽宁科技大学 A kind of desulphurization denitration active carbon and preparation method thereof
CN109384228B (en) * 2018-11-08 2020-10-09 辽宁科技大学 Desulfurization and denitrification active carbon and preparation method thereof
CN110917833A (en) * 2019-12-13 2020-03-27 西安润川环保科技有限公司 Novel flue gas denitration method
CN114044515A (en) * 2021-11-04 2022-02-15 中欣环保科技有限公司 Preparation method of desulfurization and denitrification activated carbon
CN114044515B (en) * 2021-11-04 2024-04-26 中欣环保科技有限公司 Preparation method of desulfurization and denitrification active carbon

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Address after: 030008 Shanxi province Taiyuan Xinlan Road No. 33

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