CN1820818A - Low ash coal dewatering method of hydrophobic aggregating and pelletizing to aid filtering - Google Patents
Low ash coal dewatering method of hydrophobic aggregating and pelletizing to aid filtering Download PDFInfo
- Publication number
- CN1820818A CN1820818A CN 200610037994 CN200610037994A CN1820818A CN 1820818 A CN1820818 A CN 1820818A CN 200610037994 CN200610037994 CN 200610037994 CN 200610037994 A CN200610037994 A CN 200610037994A CN 1820818 A CN1820818 A CN 1820818A
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- China
- Prior art keywords
- coal
- dewatering
- coal tar
- hydrophobic
- filter
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- 239000003245 coal Substances 0.000 title claims abstract description 35
- 230000002209 hydrophobic effect Effects 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title abstract description 10
- 238000001914 filtration Methods 0.000 title abstract description 4
- 230000004931 aggregating effect Effects 0.000 title abstract 2
- 238000005453 pelletization Methods 0.000 title abstract 2
- 239000011280 coal tar Substances 0.000 claims abstract description 25
- 239000003250 coal slurry Substances 0.000 claims abstract description 9
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000006185 dispersion Substances 0.000 claims abstract description 5
- 238000007873 sieving Methods 0.000 claims abstract description 3
- 238000004945 emulsification Methods 0.000 claims description 15
- 238000005054 agglomeration Methods 0.000 claims description 12
- 230000002776 aggregation Effects 0.000 claims description 12
- 238000005469 granulation Methods 0.000 claims description 12
- 230000003179 granulation Effects 0.000 claims description 12
- 239000000084 colloidal system Substances 0.000 claims description 8
- 239000003995 emulsifying agent Substances 0.000 claims description 6
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- ADXNPXDFKKWVGE-UHFFFAOYSA-N n,n-dimethyltridecan-1-amine Chemical group CCCCCCCCCCCCCN(C)C ADXNPXDFKKWVGE-UHFFFAOYSA-N 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 229920002472 Starch Polymers 0.000 claims description 2
- 238000005461 lubrication Methods 0.000 claims description 2
- 235000019698 starch Nutrition 0.000 claims description 2
- 239000008107 starch Substances 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 3
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000000853 adhesive Substances 0.000 abstract 1
- 230000001070 adhesive effect Effects 0.000 abstract 1
- 238000002203 pretreatment Methods 0.000 abstract 1
- 238000010008 shearing Methods 0.000 abstract 1
- 230000018044 dehydration Effects 0.000 description 12
- 238000006297 dehydration reaction Methods 0.000 description 12
- 239000000047 product Substances 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000011085 pressure filtration Methods 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 2
- 239000002817 coal dust Substances 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000010721 machine oil Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000011028 pyrite Substances 0.000 description 2
- 229910052683 pyrite Inorganic materials 0.000 description 2
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 2
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000001404 mediated effect Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The low ash coal dewatering process is especially suitable for preparing high grade active carbon with low ash coal. The dewatering process includes the following steps: adding emulsified coal tar and mixing in a high shearing dispersion machine to complete pre-treatment for hydrophobic aggregating and pelletizing of the floated fine coal slurry resulting easy dewatering of coal; and pressurizing filtering or vibration sieving the pre-treated coal slurry to dewater and to obtain product with water content of about 10 %. The product may be kneaded, formed, carbonized and activated directly to produce high grade active carbon. The coal tar serves as both filtering aid and adhesive, and can lower the water content in the product and promote the recovery of filter aid. The present invention has simple technological process, low cost, environment friendship, low power consumption and high dewatering rate.
Description
One, technical field
The present invention relates to the low culm dewatering that hydrophobic agglomeration granulation helps filter, be particularly useful for low culm and prepare top-grade active carbon.
Two, background technology
China is world's coal first big country, and coal accounts for about 75% in the primary energy consumption structure.Along with the continuous development of national economy, coal product has been proposed more and more higher requirement, particularly, also more and more higher to the requirement of moisture in coal.Because difficult separation coal is many in China's raw coal, the ratio of high ash, high sulphur content is great, further reduce the ash content and the sulphur content of floatation clean coal, improve the rate of recovery of cleaned coal, one-tenth ash mineral and pyrite in the coal are fully dissociated, for this reason must coal dust is broken, this has just increased the amount that needs the Bed for Fine Coal of processing.Especially in needing the ultralow culm preparation technology of heavily desulfurating and reducing ash, must be with coal dust broken and be milled down to tens microns even several micron, utilize advanced sorting technology can remove the ash content and the pyrite of the overwhelming majority again, make satisfactory ultralow culm.Because ultralow grey coal particle size is very thin, and the requirement to moisture is very high, as the ultralow culm moisture requirement of active carbon raw material about 10%, and the product moisture that traditional process equipment is handled is too high, for satisfying technological requirement, have only and adopt dry (oven dry is handled) dehydration, moisture is reduced to below 10%, but the cost of this drying and dehydrating is too high.
Conventional dewatering type has mechanical dehydration, and it has mainly comprised several forms such as vacuum filtration, press filtration and pressure filtration.Mechanical dehydration is present most economical dewatering type, so practical application is more, but mechanical dehydration is for the dehydration of the particularly ultra-fine grain of fine material, and effect is not fine.The filter aid dehydration also is a kind of dewatering type commonly used in addition, several modes such as inorganic type filter aid, surfactant type filter aid and flocculation formulation filter aid are arranged, change the characteristic of coal particle surface by the interpolation filter aid, moisture is wherein removed easily, the filter aid dehydration can effectively reduce product moisture, but has the problems such as character that filter aid reclaims difficulty, production cost is high and do not make full use of coal.If filter aid does not reclaim and will influence product quality, medicament wherein also can exert an influence to subsequent technique, and therefore strengthening fine coal dewatering is a problem anxious to be solved in the coal industry.
Three, summary of the invention
In view of the problem that prior art exists, the purpose of this invention is to provide a kind of reduction dehydration difficulty, simplify technological process, the hydrophobic agglomeration granulation that reduces the active carbon manufacturing cost helps the low culm dewatering of filter.
The hydrophobic agglomeration granulation of the present invention helps the low culm dewatering of filter, select floatation clean coal for use, and before floatation clean coal filters, add emulsification coal tar, adopt the high shear dispersion machine that it is mixed to stir and finish preliminary treatment, make floatation clean coal starch hydrophobic reunion, be convenient to moisture in coal and easily deviate from.Pretreated coal slurry material is positioned in the drainage bin (filter), dewaters, obtain moisture and be lower than 10% product with pressing filter or shaking-sieving mode.Emulsification coal tar is formulated by coal tar, water and dodecyl trimethyl amine bromide emulsifier; The preliminary treatment of emulsification coal tar, at first start the high shear dispersion machine and carry out preheating and oil lubrication, guarantee sound abrasive disc temperature in the time of 80 ℃～100 ℃, shutdown is preheating to 60 ℃ of coal tar, water and dodecyl trimethyl amine bromide emulsifying agent by the mass ratio adding, starts colloid mill and carries out interior circulation; The concentration that adds the emulsification coal tar in the floatation clean coal slurry is in the floatation clean coal slurry of 200g/L, adds the emulsification coal tar that accounts for cleaned coal total amount 30%.
The hydrophobic agglomeration granulation of the present invention helps the low culm dewatering of filter, is best suited for low culm and prepares top-grade active carbon.Before floatation clean coal filters, add emulsification coal tar filter aid and carry out preliminary treatment, make coal slurry hydrophobic reunion earlier, strengthen the dehydration of fine beans with this, carrying out pressurizing and dehydrating again filters, just moisture can be reduced in the claimed range, product can directly be mediated, moulding, charing, activating process.Coal tar has played filter aid and two kinds of effects of binding agent, and it not only can reduce product moisture, and helps the recovery of filter aid, has simplified technology, solved the cost problem that a large amount of filter aids bring, its method is simple, environmental protection, low energy consumption, high dehydration rate has practicality widely.
Four, the specific embodiment
The hydrophobic agglomeration granulation of the present invention helps the low culm dewatering of filter, mechanical dehydration and filter aid dehydration are combined, at first as filter aid the material that will filter is carried out hydrophobic agglomeration granulation with coal tar, carry out pressure filtration by pressing filter again, obtain moisture and be lower than 10% product, with product directly mix, moulding, charing, activating process, can obtain final products-novel high-grade active carbon.Because the coal tar flowability is very poor, must carry out emulsification treatment with before it, the emulsification treatment of coal tar adopts colloid mill to finish, earlier additional proportion is about 2 kilograms of 1: 2 machine oil and a diesel oil in colloid mill, start colloid mill, turned round 5～8 minutes, guarantee that sound abrasive disc temperature is in the time of 80 ℃～100 ℃, stop colloid mill, bleed off machine oil and diesel oil, to be preheating to 60 ℃ coal tar in the ratio that in mass ratio is 60: 40: 0.3, circulation is 0.5～1 minute in carrying out in water and the dodecyl trimethyl amine bromide emulsifying agent adding colloid mill, by coal tar is carried out emulsification treatment, makes its flowability strengthen, thereby guaranteed that coal tar can fully contact with coal particle, and, be the enough energy of hydrophobic granule at the abundant drawout of coal particle surface, formed the strong hydrophobic granule of hydrophobicity.Carry out hydrophobic reunion in the emulsification coal tar adding floatation clean coal that will make, the concentration of adding is in the coal slurry of 200g/L, adds the emulsification coal tar that accounts for cleaned coal total amount 30%, uses the high shear dispersion machine, under the 1000rpm mixing intensity, mixes stirring 20min and gets final product.Carry out pressure filtration then,, under the 0.5MPa pressure condition, carry out pressure filtration, can obtain moisture at the product below 10% with the coal slurry of hydrophobic reunion.
Claims (5)
1. hydrophobic agglomeration granulation helps the low culm dewatering of filter, it comprises the coal slurry material is positioned in the drainage bin (filter), dewater with pressing filter or shaking-sieving mode, obtain moisture and be lower than 10% product, it is characterized in that: select floatation clean coal for use, and before floatation clean coal filters, add emulsification coal tar, adopt the high shear dispersion machine that it is mixed to stir and finish preliminary treatment, make floatation clean coal starch hydrophobic reunion, be convenient to moisture in coal and easily deviate from.
2. help the low culm dewatering of filter according to right 1 described hydrophobic agglomeration granulation, it is characterized in that: described emulsification coal tar is formulated by coal tar, water and emulsifier.
3. help the low culm dewatering of filter according to right 2 described hydrophobic agglomeration granulation, it is characterized in that: described emulsifying agent is a dodecyl trimethyl amine bromide.
4. help the low culm dewatering of filter according to right 1,2 or 3 described hydrophobic agglomeration granulation, it is characterized in that: the preliminary treatment of described emulsification coal tar, at first start colloid mill and carry out preheating and oil lubrication, guarantee that sound abrasive disc temperature is in the time of 80 ℃～100 ℃, be preheating to 60 ℃ of coal tar, water and heat emulsifiers by the mass ratio adding, start colloid mill and carry out interior circulation.
5. help the low culm dewatering of filter according to right 1 described hydrophobic agglomeration granulation, it is characterized in that: described is in the floatation clean coal of 200g/L in concentration, adds the emulsification coal tar that accounts for cleaned coal total amount 30%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200610037994XA CN100368053C (en) | 2006-01-20 | 2006-01-20 | Low ash coal dewatering method of hydrophobic aggregating and pelletizing to aid filtering |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200610037994XA CN100368053C (en) | 2006-01-20 | 2006-01-20 | Low ash coal dewatering method of hydrophobic aggregating and pelletizing to aid filtering |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1820818A true CN1820818A (en) | 2006-08-23 |
| CN100368053C CN100368053C (en) | 2008-02-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200610037994XA Expired - Fee Related CN100368053C (en) | 2006-01-20 | 2006-01-20 | Low ash coal dewatering method of hydrophobic aggregating and pelletizing to aid filtering |
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| Country | Link |
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| CN (1) | CN100368053C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101653674B (en) * | 2008-08-19 | 2011-11-16 | 沈阳铝镁设计研究院有限公司 | Liquid-solid separation process and system for suspending liquid |
| CN108753388A (en) * | 2018-06-28 | 2018-11-06 | 郑翔书 | A kind of preparation method of water-coal-slurry |
| WO2023134612A1 (en) * | 2022-01-17 | 2023-07-20 | 重庆四季金标科技有限公司 | Lignite modification and dehydration method, production process thereof, and application of modified dehydrated lignite |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59105089A (en) * | 1982-12-06 | 1984-06-18 | Harima Kasei Kogyo Kk | Granulation of coal powder in water |
| US5379902A (en) * | 1993-11-09 | 1995-01-10 | The United States Of America As Represented By The United States Department Of Energy | Method for simultaneous use of a single additive for coal flotation, dewatering, and reconstitution |
| US20020144928A1 (en) * | 2001-01-29 | 2002-10-10 | Bronshtein Alexander P. | Energy efficient process for converting refinery and petroleum-based waste to standard fuels |
| US20020166794A1 (en) * | 2001-01-29 | 2002-11-14 | Bronshtein Alexander P. | Apparatus and process for converting refinery and petroleum-based waste to standard fuels |
-
2006
- 2006-01-20 CN CNB200610037994XA patent/CN100368053C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101653674B (en) * | 2008-08-19 | 2011-11-16 | 沈阳铝镁设计研究院有限公司 | Liquid-solid separation process and system for suspending liquid |
| CN108753388A (en) * | 2018-06-28 | 2018-11-06 | 郑翔书 | A kind of preparation method of water-coal-slurry |
| WO2023134612A1 (en) * | 2022-01-17 | 2023-07-20 | 重庆四季金标科技有限公司 | Lignite modification and dehydration method, production process thereof, and application of modified dehydrated lignite |
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| Publication number | Publication date |
|---|---|
| CN100368053C (en) | 2008-02-13 |
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