CN1309081A - Super-strong decoloured activated carbon block from anthracite and its preparing process - Google Patents
Super-strong decoloured activated carbon block from anthracite and its preparing process Download PDFInfo
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- CN1309081A CN1309081A CN 00100798 CN00100798A CN1309081A CN 1309081 A CN1309081 A CN 1309081A CN 00100798 CN00100798 CN 00100798 CN 00100798 A CN00100798 A CN 00100798A CN 1309081 A CN1309081 A CN 1309081A
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- activated carbon
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Abstract
A super-strong decoloured activated carbon is prepared from anthracite as main raw material, catalyst and binder through crushing, proportioning, heating while stirring, die pressing to make it become blocks, drying, activating by carbonifying, grinding and sieving. Its advantages are low cost, large specific surface area, rich macropores and mesopores and high adsorption power.
Description
The present invention relates to a kind of activated carbon and preparation method thereof, particularly a kind of super-strong decoloured activated carbon block from anthracite and preparation method thereof.
Activated carbon has the good adsorption performance, can be used for liquid phase adsorption, comprises decolouring, takes off flavor etc., and industrial, particularly environmental protection, food, medicine and military field are used very extensive.Prior art is plain particles activated carbon, column and briquetting, compressing tablet activated carbon for example, its weak point is: its specific surface area is lower, the void distribution broad, and mesopore, macropore are undeveloped, pore volume is lower, can not satisfy growing to activated carbon requirement in the use; In addition, in the prior art, all use bituminous coal to make activated carbon, the price of bituminous coal is more expensive, and the quality of bituminous coal has certain restriction to making activated carbon, and usable range is narrower, and the activated carbon quality depends on that to a great extent raw material is the natural components of bituminous coal.
The purpose of this invention is to provide a kind of super-strong decoloured activated carbon block from anthracite, it can satisfy the deficiencies in the prior art, the specific surface area that is it is higher, the void distribution broad, mesopore, macropore prosperity, pore volume height, can satisfy growing high performance requirements, and its product price is lower to activated carbon.
The objective of the invention is to realize by following technical scheme.It is raw material with the hard coal, and caking agent, catalyzer are made in addition, comprise following components in percentage by weight:
Caking agent 16-24 catalyzer 1.5-3.5
The hard coal surplus adds to 100
It is made by following technological process:
1 pulverizes.With the hard coal fragmentation, wear into fine powder.
2 batchings.By weight percentage described caking agent, catalyzer, hard coal are got ready.
3 heated and stirred.The above-mentioned material of getting ready is mixed, and heated and stirred makes it even.
4 strike out piece.The compound that above-mentioned heated and stirred finishes is put into the mould impact briquetting.
5 dryings.The briquetting that will be finished by moulding is in addition dry.
6 activation.The exsiccant briquetting is put into the activation furnace heat-activated.
7 fragmentations.After the cooling, with above-mentioned briquetting fragmentation, screen to desired particle size.
8 packings are produced.
It is main raw material that the present invention adopts hard coal, and it is handled with denatured technology, is about to mix with caking agent in the pulverized anthracite make it coalescent, mixes with catalyzer to claim pore forming agent that its specific surface area is increased again big central hole structure prosperity.By heated and stirred with add and be pressed into piece and make it reach the sex change condition.Then briquetting is placed in the activation furnace and activates, again this briquetting is crushed to desired particle size the finished product carbon dust.
The present invention adopts steady quality, ashes lower, adopting cheap hard coal is main raw material, its cost is reduced, but hard coal belongs to aging coal, it is lower that it contains the volatilization composition, hole after the activation is undeveloped, therefore can not satisfy the high performance requirements in the use, need to adopt denaturing treatment, it be reached possess mesopore, macropore prosperity, structural condition that specific surface area is big, carbonization-activation in addition in activation furnace becomes it and has high performance activated carbon then.By denaturing treatment measure of the present invention, make the cheap hard coal that is easy to obtain be able to main raw material as activated carbon, and the activated carbon after the processing greatly improves on performance than prior art bituminous coal activated carbon, as the prosperity of macropore mesopore, specific surface area increases, and the macropore prosperity can play the effect of transportation channel, makes the molecule that is adsorbed enter granule interior easily, the mesopore prosperity is used for removing the particle that has macromolecular foreign pigment or have colloidal dispersion degree from solution.In sugar industry, liquid glucose contains different coloring matters, and as caramel, melanoidin and iron content polyphenol complex compound etc., the strongest color is produced by micelle.The activated carbon that adopts the present invention to make of hard coal has very strong adsorption bleaching deodorization functions, can improve the absorption quality greatly, reaches refining purpose, and can reduce the consumption of activated carbon greatly.
In sum, the present invention enlarges markedly its specific surface area because the hard coal that has adopted cheap stable performance as raw material, by denaturing treatment, activation, is greatly improved its performance, and absorption property greatly improves, and it is cheap.Can satisfy the growing high performance requirements to activated carbon, activated carbon of the present invention is suitable for various liquid adsorption, filtration, decolouring, deodorizing use.Especially be suitable for the usefulness made from extra care.
Do concrete introduction with embodiment below.
Embodiment is an example with the broken activated carbon of briquetting,
With asphalt powder as binding agent, with potassium hydroxide as catalyzer in order to increase specific surface area, make by following step preface as raw material with the hard coal after handling through coal gangue:
1 pulverizes.With the hard coal fragmentation, it is stand-by to wear into 200 purpose fine powders.
2 batchings.Choose following component by weight percentage:
Asphalt powder 22 potassium hydroxide, 2.5 pulverized anthracite surpluses (adding to 100)
3 heated and stirred.With mixing in the above-mentioned material adding mixing machine for preparing, in whipping process, feed steam heating, 110 ℃ of temperature, until stirring, are sent to immediately and are struck out piece 30 minutes time.
4 strike out piece.In the mould of porous, shaped machine, this material of punching press becomes piece shape.Temperature is 80 ℃ during punching press, and pressure is 7000Mpa.
5 dryings.Will be in addition dry by the briquetting of moulding.
6 activation.In the physically activated stove of STK the exsiccant briquetting put into and carry out the carbon activation, 900 ℃ of vapor pressures of Heating temperature are 0.3Mpa, residing time in furnace 52 hours, adopt the regularly reinforced discharging of continuous oven.
7 fragmentations.Above-mentioned briquetting is cooled off fragmentation, wears into required particle,, dispatch from the factory as product activated carbon powder packing through screening to desired particle size.Activated carbon powder can be processed into the activated carbon block use of different shape.
Activated carbon price of the present invention is lower, through performance test, with existing activated carbon phase of making of bituminous coal Ratio, performance improves, and is as shown in table 1. Table 1
It is as shown in the table, and anthracite activated carbon of the present invention is owing to adopt denatured technology to make its indices all excellent In common bituminous coal activated carbon, its adsorption capacity to serge blue, iodine, carbon tetrachloride all is better than common cigarette Coal activity carbon. Particularly the pore volume value is greater than one times of common bituminous coal activated carbon, and water capacity, specific surface Long-pending value is about 1.5 times of common bituminous coal activated carbon, and anthracite activated carbon of the present invention does not have floating thing.
Claims (7)
1, a kind of super-strong decoloured activated carbon block is characterized in that: it is raw material with the hard coal, and caking agent, catalyzer are made in addition, comprise following components in percentage by weight:
Caking agent 16-24 catalyzer 1.5-3.5
The hard coal surplus adds to 100
2, super-strong decoloured activated carbon block according to claim 1 is characterized in that: it is made by following technological process:
(1) pulverizes.With the hard coal fragmentation, wear into fine powder.
(2) batching.By weight percentage described caking agent, catalyzer, hard coal are got ready.
(3) heated and stirred.The above-mentioned material of getting ready is mixed, and heated and stirred makes it even.
(4) strike out piece.The compound that above-mentioned heated and stirred finishes is put into the mould impact briquetting.
(5) drying.The briquetting that will be finished by moulding is in addition dry.
(6) activation.The exsiccant briquetting is put into the activation furnace heat-activated.
(7) fragmentation.After the cooling, with above-mentioned briquetting fragmentation, screen to desired particle size.
(8) packing is produced.
3, super-strong decoloured activated carbon block according to claim 1 and 2 is characterized in that: described caking agent is an asphalt powder.
4, super-strong decoloured activated carbon block according to claim 1 and 2 is characterized in that: described catalyzer is a potassium hydroxide.
5, super-strong decoloured activated carbon block according to claim 2 is characterized in that: in described technological process (3), feed steam, temperature 100-130 ℃, 25-35 minute heat-up time during heated and stirred.
6, super-strong decoloured activated carbon block according to claim 2 is characterized in that: in described technological process (4), its temperature is 60-120 ℃, and pressure is 7000Mpa.
7, super-strong decoloured activated carbon block according to claim 2 is characterized in that: in described technological process (6), the feeding temperature is 800-950 ℃ a steam heating, and vapor pressure is 0.25-0.35Mpa, and be 44-60 hour heat-up time.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB00100798XA CN1145584C (en) | 2000-02-14 | 2000-02-14 | Super-strong decoloured activated carbon block from anthracite and its preparing process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB00100798XA CN1145584C (en) | 2000-02-14 | 2000-02-14 | Super-strong decoloured activated carbon block from anthracite and its preparing process |
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| Publication Number | Publication Date |
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| CN1309081A true CN1309081A (en) | 2001-08-22 |
| CN1145584C CN1145584C (en) | 2004-04-14 |
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| CNB00100798XA Expired - Fee Related CN1145584C (en) | 2000-02-14 | 2000-02-14 | Super-strong decoloured activated carbon block from anthracite and its preparing process |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101503191B (en) * | 2009-03-13 | 2011-01-12 | 北京化工大学 | Method for preparing honeycomb active carbon from coal and coal tar |
| CN102432004A (en) * | 2011-09-22 | 2012-05-02 | 煤炭科学研究总院 | Active carbon for deeply purifying drinking water and preparation method thereof |
| CN102530938A (en) * | 2011-12-29 | 2012-07-04 | 大同煤矿集团有限责任公司 | Method for producing drinking water deep purification activated carbon by utilizing Datong coal |
| CN104528717A (en) * | 2015-02-01 | 2015-04-22 | 庄林生 | Preparation method of briquetted active carbon |
| CN105419876A (en) * | 2015-11-30 | 2016-03-23 | 新奥科技发展有限公司 | Anthracite pretreatment method |
| CN105693501A (en) * | 2016-04-29 | 2016-06-22 | 南通大学 | Activated carbon briquette for potassium sorbate decoloring and preparation method thereof |
| CN105712869A (en) * | 2016-04-29 | 2016-06-29 | 南通大学 | Activated carbon press block for sorbic acid decoloration and preparation method thereof |
| CN112551921A (en) * | 2020-11-25 | 2021-03-26 | 海城远东矿业有限公司 | Carbonization activation beneficiation technology for high-silicon magnesite |
-
2000
- 2000-02-14 CN CNB00100798XA patent/CN1145584C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101503191B (en) * | 2009-03-13 | 2011-01-12 | 北京化工大学 | Method for preparing honeycomb active carbon from coal and coal tar |
| CN102432004A (en) * | 2011-09-22 | 2012-05-02 | 煤炭科学研究总院 | Active carbon for deeply purifying drinking water and preparation method thereof |
| CN102432004B (en) * | 2011-09-22 | 2013-12-25 | 煤炭科学研究总院 | Active carbon for deeply purifying drinking water and preparation method thereof |
| CN102530938A (en) * | 2011-12-29 | 2012-07-04 | 大同煤矿集团有限责任公司 | Method for producing drinking water deep purification activated carbon by utilizing Datong coal |
| CN104528717A (en) * | 2015-02-01 | 2015-04-22 | 庄林生 | Preparation method of briquetted active carbon |
| CN105419876A (en) * | 2015-11-30 | 2016-03-23 | 新奥科技发展有限公司 | Anthracite pretreatment method |
| CN105419876B (en) * | 2015-11-30 | 2018-04-20 | 新奥科技发展有限公司 | A kind of anthracitic preprocess method |
| CN105693501A (en) * | 2016-04-29 | 2016-06-22 | 南通大学 | Activated carbon briquette for potassium sorbate decoloring and preparation method thereof |
| CN105712869A (en) * | 2016-04-29 | 2016-06-29 | 南通大学 | Activated carbon press block for sorbic acid decoloration and preparation method thereof |
| CN105693501B (en) * | 2016-04-29 | 2018-03-27 | 南通大学 | Activated carbon briquetting to be decolourized for potassium sorbate and preparation method thereof |
| CN112551921A (en) * | 2020-11-25 | 2021-03-26 | 海城远东矿业有限公司 | Carbonization activation beneficiation technology for high-silicon magnesite |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1145584C (en) | 2004-04-14 |
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