CN100372916C - Environment protection and quality increasing process for coal and water-coal fluid - Google Patents
Environment protection and quality increasing process for coal and water-coal fluid Download PDFInfo
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- CN100372916C CN100372916C CNB2005100214815A CN200510021481A CN100372916C CN 100372916 C CN100372916 C CN 100372916C CN B2005100214815 A CNB2005100214815 A CN B2005100214815A CN 200510021481 A CN200510021481 A CN 200510021481A CN 100372916 C CN100372916 C CN 100372916C
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- 239000003245 coal Substances 0.000 title claims abstract description 74
- 238000000034 method Methods 0.000 title claims abstract description 16
- 230000008569 process Effects 0.000 title claims abstract description 10
- 239000012530 fluid Substances 0.000 title 1
- 239000002002 slurry Substances 0.000 claims abstract description 30
- 239000000843 powder Substances 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000002245 particle Substances 0.000 claims abstract description 18
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000011593 sulfur Substances 0.000 claims abstract description 9
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 9
- 239000003795 chemical substances by application Substances 0.000 claims description 16
- 230000003009 desulfurizing effect Effects 0.000 claims description 16
- 230000007613 environmental effect Effects 0.000 claims description 12
- 238000003672 processing method Methods 0.000 claims description 12
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical group [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 8
- 239000002817 coal dust Substances 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 7
- 239000005864 Sulphur Substances 0.000 claims description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 5
- 239000011707 mineral Substances 0.000 claims description 5
- 208000001840 Dandruff Diseases 0.000 claims description 4
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 4
- 239000012535 impurity Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 8
- 239000000654 additive Substances 0.000 abstract description 6
- 230000000996 additive effect Effects 0.000 abstract description 6
- 238000006477 desulfuration reaction Methods 0.000 abstract description 5
- 230000023556 desulfurization Effects 0.000 abstract description 5
- 239000000779 smoke Substances 0.000 abstract description 3
- 239000007789 gas Substances 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000011882 ultra-fine particle Substances 0.000 abstract 4
- 239000007921 spray Substances 0.000 abstract 1
- 239000000446 fuel Substances 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 241000276489 Merlangius merlangus Species 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000003250 coal slurry Substances 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 239000003818 cinder Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 241001417490 Sillaginidae Species 0.000 description 2
- 238000005703 Whiting synthesis reaction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229910052742 iron Inorganic materials 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
- 239000011028 pyrite Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000219051 Fagopyrum Species 0.000 description 1
- 235000009419 Fagopyrum esculentum Nutrition 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000009837 dry grinding Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 235000012204 lemonade/lime carbonate Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000003765 sweetening agent Substances 0.000 description 1
- 238000001238 wet grinding Methods 0.000 description 1
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- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The present invention discloses an environment protection and quality increasing process for coal, which comprises the following steps: 1) treating coal with an ultra-fine device so as to pulverize the coal into ultra-fine particles in submicron size; 2) uniformly mixing the ultra-fine particles with a desulfurization additive according to the sulfur content of the ultra-fine particles. The present invention also discloses coal water slurry which comprises coal powder and the desulfurization additive, wherein the coal powder has the average particle size less than 1.8 mu m, and the desulfurization additive has the average particle size less than 2.0 mu m. The present invention has the advantages that the particle surface activity is greatly improved after the coal powder is pulverized into the ultra-fine particles, so that the combustion can proceed rapidly and completely, the combustion utilization rate of the coal is effectively enhanced and the discharge of harmful gases is correspondingly reduced; meanwhile, the coal powder particles are pulverized into the submicron size so as to make the surface area increased by multiple times, so that the coal powder particles can better react with the desulfurization additive and the sulfur content in smoke is reduced; due to the ultra-fine coal particles, the blockage of a spray nozzle in the combustion process is effectively reduced.
Description
[technical field]
The present invention relates to the deep processing of natural resources, be specifically related to a kind of environmental protection and high quality processing method and coal water slurry of coal.
[background technology]
Coal and oil all are the human extensive conventional energy resourcess that use, and wherein the reserves of coal are the abundantest, are about 20 times of oil.In the Energy resources reserves of China, coal accounts for more than 84%, has huge potentiality to be exploited.From the angle of resource provisioning, the coal resources that China is last hundreds of millions tons can satisfy huge energy increased requirement in Chinese 100 years fully, and substitutes the nonessential petroleum demand of a part.And in actual use, coal accounts for more than 70% in energy structure in China also really in occupation of leading status.Coal resources exploitations is convenient, but compares with oil or a lot of inferior places are arranged: solid fuel, and transportation inconvenience, efficiency of combustion is low, and lime-ash is many, contaminate environment.In China, the coal utilization mode is still based on burning.In order to improve burning of coal efficient, in the international petroleum time of crisis at the end of the seventies high-new technology products---coal water slurry has appearred.It is by about 70% coal, and the outward appearance that about 30% water and a small amount of additive are formed is like the petroleum supplements of heavy oil, and its mode of production is milled down to about 200 orders with ball mill after coal is added water.COAL-WATER SLURRY TECHNOLOGY becomes coal derived fuel with solid-state coal fuel, the fuel characteristic that had both kept coal, the liquid due characteristics that possessed similar heavy oil again, replacing fuel with it as heavy oil is that a kind of preparation is simple, being convenient to transportation stores, one of safe and reliable novel clean fuel has obtained industrial application in developed country.But this coal water slurry is big to the wearing and tearing of burner noz(zle), also easy plug nozzle.In addition, in the burning of coal process, also a large amount of sulfur-containing smoke gas be can produce, serious acid rain and dust pollution caused.At present both at home and abroad in the burning of coal desulfurization, the most ripe method that effectively still adds sweetening agent of employing, lime carbonate for example, but because the reaction table area is little often needs the amount that adds bigger, and reaction also is difficult to fully.
[summary of the invention]
The objective of the invention is to propose a kind of environmental protection and the high quality processing method and coal water slurry that can in use effectively improve efficiency of combustion and reduce the coal of discharging amount of sulfur contenting in smoke.
A technical scheme that realizes above-mentioned purpose is: a kind of environmental protection of coal and high quality processing method comprise the steps:
1) adopts ultra-fine equipment that coal is carried out the ultra micro thinning processing, it is crushed to submicron-scale;
2) add desulfurizing assistant agent according to its sulphur content in the coal after ultra-fine processing, mix.
Described step 1) can adopt and comprise that following several process step by step realizes:
1a), then directly carry out next step,, then earlier it is roughly ground, make the satisfactory powder of granularity if its fineness is lower than the charging requirement of ultra-fine equipment if the fineness of coal satisfies the charging requirement of ultra-fine equipment;
1b) above-mentioned powder is made solid content and be not less than 40% slurry;
1c) use ultra-fine equipment that slurry is ground, make that powder granularity is 0.1 μ m～1.8 μ m.
Step 1a) the preferred high pressure roll-in mill that uses in, it is 200～325 purpose powders that raw material is made granularity.
Described step 1c) in, preferably uses the super-fine whirl mill, in the process that grinds, the impurity that contains sulfur mineral (for example pyrite) comprising in the raw material is separated as ultra-fine equipment.The mean particle size that ultra-fine equipment is pulverized the back powder is preferably 0.12～0.45 μ m.
Preferably, described step 2) desulfurizing assistant agent that adds in passes through the ultra micro thinning processing equally, and mean particle size is less than 2.0 μ m.
Another technical scheme that realizes the object of the invention is, a kind of coal water slurry comprises coal dust and desulfurizing assistant agent, and the mean particle size of described coal dust is less than 1.8 μ m, and the mean particle size of described desulfurizing assistant agent is less than 2.0 μ m.
Described desulfurizing assistant agent can be selected calcium carbonate powders.
Adopt technique scheme, beneficial technical effects of the present invention is: after 1) coal dust being carried out ultra-fine processing, improved the particulate surfactivity greatly, make combustion reactions to carry out completely rapidly, effectively improve the burning of coal utilization ratio, and burning completely also helps the minimizing of obnoxious flavour.Pulverized coal particle is ultra-fine to submicron-scale simultaneously, and specific surface area has increased thousands of times, can better react with desulfurizing assistant agent, reduces the sulphur content in the flue gas.2) desulfurizing assistant agent is also carried out ultra-fine processing, make its increased activity desulphurization reaction, not only can significantly promote its sulfur limitation effect, can also reduce the auxiliary agent usage quantity, reduce the generation of by product, environmental protection more economically more fast with complete.3) use high pressure roll-in mill that coal dust is carried out coarse grinding treatment, because coal dust has passed through the pressure of high pressure roller pressure device, each buckwheat coal is inner can to produce a lot of stress defectives, becomes a kind of tiny crack, helps these coarse grain and is further pulverized in follow-up ultra-fine process.4) use the super-fine whirl mill can finish superfine grinding, can also make impurity contained in the coal, as sulfur-bearing mineral yellow iron ore, in the eddy flow mill, separate, raw material further obtains purifying, improve the effective rate of utilization of burning material,, thereby effectively reduced the SO2 content in the flue gas of burning back simultaneously owing to before burning, removed sulfur-bearing mineral yellow iron ore.
Below by specific embodiment, the present invention is described in further detail:
[embodiment]
A kind of high quality processing method of ceramic pigment, its technical process is:
1) at first adopts ultra-fine equipment that coal is carried out the ultra micro thinning processing, it is crushed to submicron-scale.
Generally speaking, the mineral coal that exploitation is come out all has large-size, can not directly enter ultra-fine equipment and pulverize, and can be earlier roughly grinds through ball mill such as Raymond mill or high pressure roll-in mill, to make ultra-fine equipment acceptable powder.Wherein high pressure roll-in mill is particularly preferred, and not only energy consumption is low, and can make the inner stress crack that produces of the rough coal powder that makes, and helps follow-up ultra-fine step.According to the requirement of existing general ultra-fine equipment, the granularity of charging powder all allows between 200～325 orders.
Difference according to the mode of operation of ultra-fine equipment, equipment for wet grinding also will be made powder the slurry that meets its requirement, general solid content all is being feasible more than 40%, comparatively suitable between 65%～75%, when the slurry solid content is 100%, then be suitable for the ultra-fine equipment of dry grinding.
As for the selection of ultra-fine equipment, can carry out ultra-fine equipment such as general optional stirring mill, vibration mill, airflow milling according to the characteristics of treatment capacity and concrete raw material.In order to realize the present invention with lower cost and energy consumption, preferably adopt the super-fine whirl mill of the present application people invention, the Chinese patent application of this invention number is 200410081580.8.This invention super-fine whirl mill is for stirring a kind of of mill, its mill tube inwall does not wait apart from the radius in axle center in the horizontal direction, thereby linear velocity difference, and have a plurality of linear velocities, make that material rotation in the horizontal direction is a speed-change process, this structure makes grinding mechanism such as shearing, extruding, collision coexist as the different sections of same inner core, so material further increases at suffered stress of corase grind stage, the internal tiny crack disintegration, can improve grinding efficiency greatly, with material ultra-fine be extremely fine particle.Simultaneously, in ultra-fine process, because the isolating effect of rotation, hydrocarbon polymer contained in the feed coal is effectively separated with ash, improves fuel purity.After ultra-fine equipment ground, the discharging powder granularity was controlled between 0.1 μ m～1.8 μ m and all is fit to, and the mean particle size of powder can reach best effect when 0.12～0.45 μ m left and right sides.
2) add desulfurizing assistant agent according to its sulphur content in the coal after ultra-fine processing, mix.Desulfurizing assistant agent is generally selected alkaline metal cpds for use, and wherein effect is preferably heavy calcium carbonate.In order to improve sweetening effectiveness, preferably the desulfurizing assistant agent that adds is also carried out the ultra micro thinning processing, make its mean particle size less than 2.0 μ m, like this when coal dust firing, a series of high-temperature chemical reactions carry out under submicron-scale, because the existence of nano effect can make that efficiency of combustion improves greatly, desulphurization reaction speed improves several times to tens times, finally is implemented in the clean and effective utilization of the coal under the low cost.Following table has been listed the various the physical-chemical parameters of traditional coal-water-slurry and submicron coal water slurry of the present invention, and by more as can be seen, coal water slurry of the present invention has remarkable advantages such as purity high thermal efficiency height.
The comparison of traditional coal-water-slurry and submicron coal water slurry of the present invention
| Ash (%) | Sulphur (%) | Maximum particle diameter (μ m) | Median size (μ m) | Viscosity (CPS) | Additive amount % | Calorific value MJ/kg | |
| Traditional coal-water-slurry | <10 | ≤0.5 | <300 | <50 | <1400 | 1 | >17 |
| The submicron coal water slurry | <1 | ≤0.15 | <1.8 | <0.45 | <300 | 0.1 | >28 |
Experimental example:
Raw material and equipment: 100 kilograms of coal cinders (colliery, Daye, Shanxi produces), 1 (WXA1 type of super-fine whirl mill, Shenzhen big male mechanical means company limited produces), 1 (WG3 type of high pressure roll-in mill, Shenzhen big male mechanical means company limited produces), 50 kilograms of 300 order water-ground limestones (Guangxi product), 1 at burner noz(zle).
The inventive method is handled:
1) getting 50 kilograms of coal cinders handles through the high pressure roller pressure device earlier, the pulpous state of the rough coal powder water furnishing solid content 70% that will handle then, enter again in the super-fine whirl mill and carry out ultra-fine processing, remove the ash and the pyrite of bottom settlings, then coal slurry is put into storage tank.
2) get 40 kilograms of 300 order coarse whitings, the pulpous state of water furnishing solid content 70% enters in the super-fine whirl mill again and carries out ultra-fine processing, then the coarse whiting slurry is put into storage tank.
3) with coal slurry and 1.5 kilograms of coarse whiting slurries thorough mixing in the eddy flow mill of 1,2 steps, burn, record SO in the flue gas by burner noz(zle)
2Concentration be 181mg/Nm
3
4) measuring the coal water slurry calorific value is 29.42MJ/kg, and efficiency of combustion is 99.6%, and boiler efficiency is 93%.
Control methods:
1) get 50 kilograms of coal cinders levigate mistake 200 mesh sieves of ball mill, the pulpous state of water furnishing solid content 70% is put into storage tank with coal slurry then;
2) get 10 kilograms of 300 order coarse whitings, the pulpous state of water furnishing solid content 70% is put into storage tank with the coarse whiting slurry then.
3) coal slurry with 1,2 steps mixes with 3 kilograms of coarse whiting slurries, burns by burner noz(zle), records SO in the flue gas
2Content be 730mg/Nm
3
4) measuring the coal water slurry calorific value is 18.91MJ/kg, and efficiency of combustion is 96%, and boiler efficiency is 87%.
Relatively the result of two kinds of treatment processs as can be seen, the ultra-thin slurries that adopts the inventive method to make has good character, is the feasible way efficiently that cleans of coal.
Claims (9)
1. the environmental protection of a coal and high quality processing method comprise the steps:
1) adopts ultra-fine equipment that coal is carried out the ultra micro thinning processing, it is crushed to submicron-scale;
2) add desulfurizing assistant agent according to its sulphur content in the coal after ultra-fine processing, mix.
2. the environmental protection of coal according to claim 1 and high quality processing method is characterized in that: the desulfurizing assistant agent that adds described step 2) passes through the ultra micro thinning processing equally, and mean particle size is less than 2 μ m.
3. the environmental protection of coal according to claim 1 and high quality processing method, it is characterized in that: described desulfurizing assistant agent is a calcium carbonate powders.
4. the environmental protection of coal according to claim 2 and high quality processing method, it is characterized in that: described step 1) comprises following step by step several:
1a), then directly carry out next step,, then earlier it is roughly ground, make the satisfactory powder of granularity if its fineness is lower than the charging requirement of ultra-fine equipment if the fineness of coal satisfies the charging requirement of ultra-fine equipment;
1b) above-mentioned powder is made solid content and be not less than 40% slurry;
1c) use ultra-fine equipment that slurry is ground, make that powder granularity is 0.1 μ m～1.8 μ m.
5. the environmental protection of coal according to claim 4 and high quality processing method is characterized in that: described step 1c), the mean particle size that ultra-fine equipment is pulverized the back powder is 0.12～0.45 μ m.
6. the environmental protection of coal according to claim 4 and high quality processing method is characterized in that: at step 1a) in use high pressure roll-in mill, it is 200～325 purpose powders that raw material is made granularity.
7. the environmental protection of coal according to claim 4 and high quality processing method is characterized in that: at step 1c) in use the super-fine whirl mill, in the process that grinds, the impurity that contains sulfur mineral comprising in the raw material is separated.
8. a coal water slurry comprises coal dust and desulfurizing assistant agent, it is characterized in that: the mean particle size of described coal dust is less than 1.8 μ m, and the mean particle size of described desulfurizing assistant agent is less than 2.0 μ m.
9. coal water slurry according to claim 8 is characterized in that: described desulfurizing assistant agent is a calcium carbonate powders.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB2005100214815A CN100372916C (en) | 2005-08-09 | 2005-08-09 | Environment protection and quality increasing process for coal and water-coal fluid |
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| CNB2005100214815A CN100372916C (en) | 2005-08-09 | 2005-08-09 | Environment protection and quality increasing process for coal and water-coal fluid |
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| CN1752192A CN1752192A (en) | 2006-03-29 |
| CN100372916C true CN100372916C (en) | 2008-03-05 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101245918B (en) * | 2008-03-21 | 2010-07-21 | 广州大华德盛科技有限公司 | Novel pulping method for hyperfine water-coal-slurry |
| US10287522B2 (en) | 2013-01-31 | 2019-05-14 | General Electric Company | System and method for preparing coal water slurry |
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| CN109539295A (en) * | 2018-12-06 | 2019-03-29 | 广东清远蒙娜丽莎建陶有限公司 | With baking sulphur intelligence feeding system in a kind of furnace |
| CN115558530B (en) * | 2022-09-23 | 2023-10-27 | 神华准能资源综合开发有限公司 | Nano hydrocarbon fuel and preparation method thereof |
| CN115449407B (en) * | 2022-09-23 | 2024-05-07 | 神华准能资源综合开发有限公司 | Environment-friendly nano hydrocarbon fuel and preparation method thereof |
| CN115746926A (en) * | 2022-12-29 | 2023-03-07 | 神华准能资源综合开发有限公司 | Nano pulverized coal, nano hydrocarbon fuel and preparation method thereof |
| CN116355663A (en) * | 2022-12-29 | 2023-06-30 | 神华准能资源综合开发有限公司 | Nanometer pulverized coal primary pulp, nanometer hydrocarbon fuel and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04314787A (en) * | 1991-04-12 | 1992-11-05 | Mitsubishi Heavy Ind Ltd | Dispersion stabilizer for coal/water slurry |
| JPH06158065A (en) * | 1992-11-30 | 1994-06-07 | Nippon Com Kk | Feeding of dispersant in production of coal/water slurry |
| US5599356A (en) * | 1990-03-14 | 1997-02-04 | Jgc Corporation | Process for producing an aqueous high concentration coal slurry |
| CN1210093A (en) * | 1997-09-04 | 1999-03-10 | 赵德山 | Closed circulation treatment of waste water and gases in papermaking plants |
-
2005
- 2005-08-09 CN CNB2005100214815A patent/CN100372916C/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5599356A (en) * | 1990-03-14 | 1997-02-04 | Jgc Corporation | Process for producing an aqueous high concentration coal slurry |
| JPH04314787A (en) * | 1991-04-12 | 1992-11-05 | Mitsubishi Heavy Ind Ltd | Dispersion stabilizer for coal/water slurry |
| JPH06158065A (en) * | 1992-11-30 | 1994-06-07 | Nippon Com Kk | Feeding of dispersant in production of coal/water slurry |
| CN1210093A (en) * | 1997-09-04 | 1999-03-10 | 赵德山 | Closed circulation treatment of waste water and gases in papermaking plants |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101245918B (en) * | 2008-03-21 | 2010-07-21 | 广州大华德盛科技有限公司 | Novel pulping method for hyperfine water-coal-slurry |
| US10287522B2 (en) | 2013-01-31 | 2019-05-14 | General Electric Company | System and method for preparing coal water slurry |
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| CN1752192A (en) | 2006-03-29 |
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