CN1908134A - High concentration sludge coal slurry and method for preparing the same - Google Patents
High concentration sludge coal slurry and method for preparing the same Download PDFInfo
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- CN1908134A CN1908134A CN 200610030071 CN200610030071A CN1908134A CN 1908134 A CN1908134 A CN 1908134A CN 200610030071 CN200610030071 CN 200610030071 CN 200610030071 A CN200610030071 A CN 200610030071A CN 1908134 A CN1908134 A CN 1908134A
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- 239000010802 sludge Substances 0.000 title claims abstract description 68
- 239000003250 coal slurry Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000003245 coal Substances 0.000 claims abstract description 22
- 238000002360 preparation method Methods 0.000 claims abstract description 19
- 239000000654 additive Substances 0.000 claims abstract description 13
- 239000000446 fuel Substances 0.000 claims abstract description 8
- 230000004048 modification Effects 0.000 claims description 16
- 238000012986 modification Methods 0.000 claims description 16
- 239000003814 drug Substances 0.000 claims description 13
- 230000000996 additive effect Effects 0.000 claims description 11
- 239000010801 sewage sludge Substances 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 239000010865 sewage Substances 0.000 claims description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 3
- 239000000920 calcium hydroxide Substances 0.000 claims description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 3
- 235000012204 lemonade/lime carbonate Nutrition 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 241000196324 Embryophyta Species 0.000 claims description 2
- 229920001732 Lignosulfonate Polymers 0.000 claims description 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical class [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 2
- 239000002802 bituminous coal Substances 0.000 claims description 2
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 2
- 239000002817 coal dust Substances 0.000 claims description 2
- 239000010842 industrial wastewater Substances 0.000 claims description 2
- 239000003077 lignite Substances 0.000 claims description 2
- 235000019357 lignosulphonate Nutrition 0.000 claims description 2
- PSZYNBSKGUBXEH-UHFFFAOYSA-M naphthalene-1-sulfonate Chemical compound C1=CC=C2C(S(=O)(=O)[O-])=CC=CC2=C1 PSZYNBSKGUBXEH-UHFFFAOYSA-M 0.000 claims description 2
- 229920005646 polycarboxylate Polymers 0.000 claims description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 2
- 235000015320 potassium carbonate Nutrition 0.000 claims description 2
- 235000017550 sodium carbonate Nutrition 0.000 claims description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 claims description 2
- 238000004065 wastewater treatment Methods 0.000 claims description 2
- 238000005086 pumping Methods 0.000 abstract description 5
- 238000002309 gasification Methods 0.000 abstract description 4
- 231100000331 toxic Toxicity 0.000 abstract description 4
- 230000002588 toxic effect Effects 0.000 abstract description 4
- 239000012530 fluid Substances 0.000 abstract description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000003381 stabilizer Substances 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract 2
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 239000000843 powder Substances 0.000 abstract 1
- 239000002002 slurry Substances 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 4
- 231100000614 poison Toxicity 0.000 description 3
- 230000007096 poisonous effect Effects 0.000 description 3
- 238000004537 pulping Methods 0.000 description 3
- 238000007669 thermal treatment Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 231100001261 hazardous Toxicity 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- XUZHLZDRCCUWEV-UHFFFAOYSA-N formaldehyde;methyl naphthalene-1-sulfonate Chemical compound O=C.C1=CC=C2C(S(=O)(=O)OC)=CC=CC2=C1 XUZHLZDRCCUWEV-UHFFFAOYSA-N 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 229920005552 sodium lignosulfonate Polymers 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
- Treatment Of Sludge (AREA)
Abstract
本发明公开了一种高浓度污泥煤浆及其制备方法。组分和重量份数含量包括：煤粉100～200份，含水污泥10～50份，水10～100份，添加剂1～5份，污泥改性药剂1～5份。本发明操作简单，耗能少，成本低，产生的二次污染少。该制备方法具有提高污泥煤浆的成浆性的优点及效果，成浆浓度可以提高到55％以上，同时表观粘度在1000MPa·s以下，无需额外投加稳定剂，长时间放置不会产生硬沉淀，并且流动性很好，适合泵送。所说的高浓度污泥煤浆可以作为燃料燃烧或气化，不仅能使污泥中的热值得到充分利用，而且还克服了现有含水污泥热处理耗能高，尾气和残渣有毒有害难治理等问题，并且制备过程中不排放大量有毒有害的尾气。The invention discloses a high-concentration sludge coal slurry and a preparation method thereof. Components and parts by weight include: 100-200 parts of coal powder, 10-50 parts of water-containing sludge, 10-100 parts of water, 1-5 parts of additives, and 1-5 parts of sludge modifying agent. The invention has the advantages of simple operation, low energy consumption, low cost and less secondary pollution. The preparation method has the advantages and effects of improving the slurrying property of the sludge coal slurry, the slurrying concentration can be increased to more than 55%, and the apparent viscosity is below 1000MPa·s, no additional stabilizer is needed, and it will not stand for a long time Produces hard deposits and is very fluid for pumping. The high-concentration sludge coal slurry can be used as fuel for combustion or gasification, which can not only make full use of the calorific value in the sludge, but also overcome the high energy consumption of the existing water-containing sludge heat treatment, and the toxic and harmful tail gas and residues. governance and other issues, and the preparation process does not emit a large amount of toxic and harmful tail gas.
Description
Technical field
The present invention relates to a kind of sludge coal slurry and preparation method thereof.
Background technology
Coal water slurry is the novel coal based fluid fuel of a kind of replace oil with coal of rising behind the world oil crisis seventies in 20th century, and making coal is a kind of fluid fuel from traditional solid fuel conversion, thereby brings lot of advantages.Coal water slurry is as oil, can pumping, atomizing, storage is with the stable ignition burning and gasify.
The reasonable processing of water-containing sludge and recycling are the key subjects of sewage disposal and environment protection.In present various water-containing sludge treatment processs, heat treating method has prospect most.Mud thermal treatment can not only be rapidly and is made mud reach minimizing largely, and can also make the calorific value in the mud obtain certain utilization.But, containing large quantity of moisture in the mud, generally can reach about 80%, existing heat treating method generally needs sludge-drying in advance, removes large quantity of moisture wherein.The dry in advance of mud needs to consume a large amount of heats, and can produce the poisonous and hazardous stench tail gas of a large amount of refractory reasons, causes existing mud heat treatment technics cost height, and power consumption is high, problems such as tail gas refractory reason.
Coal being mixed with water-containing sludge, and adopt certain technique means, with mixture preparation becoming sludge coal slurry, as fuel, is the previous very noticeable problem of order.
Pulping concentration is the most important technical indicator that influences sludge coal slurry burning and gasification efficiency.Water in the sludge coal slurry not only can not provide heat, and also can evaporate and cause thermosteresis in burning and gasification.Existing patented technology, the medicament that in the process of preparation sludge coal slurry, adds the energy modified sewage sludge as Chinese patent 200410024452.X, cause the pulping concentration of sludge coal slurry not high, generally be lower than 55wt%, cause too much thermosteresis in actual applications easily.
Stability also is to estimate one of good important parameter of sludge coal slurry, and existing patented technology need add certain amount of stabilizer as the sludge coal slurry of preparing in the Chinese patent 200410021357.4 and keep its stability.
The discharging of tail gas is the problem that very easily produces in the sludge coal slurry preparation process.Mud contains the organism of large amount of complex, very easily produces toxic and harmful after the thermal treatment.Existing patented technology, as United States Patent (USP) 99814537.8, its defective is to prepare the preceding sex change operation of sludge coal slurry and has produced toxic and harmful, has increased the technology cost of sludge coal slurry preparation.
Summary of the invention
The technical issues that need to address of the present invention are to disclose a kind of high concentration sludge coal slurry and preparation method thereof, to overcome the shortcoming and defect of above-mentioned prior art.
The component of high concentration sludge coal slurry of the present invention and parts by weight content comprise:
100～200 parts of coal dusts
10～50 parts of water-containing sludges
10～100 parts in water
1～5 part of additive
1～5 part of sludge modification medicament
Wherein, the particle diameter of solid particulate is no more than 0.5mm.
In the said water-containing sludge, water ratio is 50～95%, weight;
Described coal is selected from brown coal, bituminous coal, hard coal or its mixture;
Described water-containing sludge is selected from the sewage sludge of municipal sewage plant's generation, wastewater sludge, the paper mill effluent that Industrial Wastewater Treatment produces handled paper mill sludge or its mixture that produces;
Additive is any one or a few in naphthalenesulfonate, polycarboxylate or the sulfonated lignin;
The sludge modification medicament is any one or a few in lime carbonate, yellow soda ash, sodium bicarbonate, salt of wormwood, calcium hydroxide, sodium hydroxide or the potassium hydroxide.
The preparation method of said high concentration sludge coal slurry comprises the steps:
Water-containing sludge is mixed with the sludge modification medicament, obtain the modification water-containing sludge, preferably mix the back and placed 2～240 hours;
Then above-mentioned modification water-containing sludge, coal dust, water and additive are mixed, grind, the particle diameter that makes solid particulate promptly obtains said high concentration sludge coal slurry less than 0.5mm.
The present invention is simple to operate, and power consumption is few, and cost is low, and the secondary pollution of generation is few.This preparation method has the advantage and the effect of the sludge forming performance that improves sludge coal slurry, and pulping concentration can be brought up to more than 55%, and apparent viscosity is below 1000mPas simultaneously, need not additionally to add stablizer, long-time placement can not produce hard-caked sediment, and mobile fine, is fit to pumping.
The high concentration sludge coal slurry of the present invention's preparation can be used as fuel combustion or gasification, calorific value in the mud is fully used, but also it is high to have overcome existing water-containing sludge thermal treatment power consumption, problems such as tail gas and residue poisonous and harmful refractory reason, and do not discharge a large amount of poisonous and hazardous tail gas in the preparation process.
Embodiment
Embodiment 1
1. raw material
(1) sewage sludge of Shanghai City sewage work generation, water-content------80%, weight;
(2) certain colliery lump coal, water-content------2%, ash content------15%;
(3) additive (sodium lignosulfonate)
(4) sludge modification medicament (lime carbonate)
(5) tap water
2. preparation condition
(1) proportioning raw materials (parts by weight)
100 parts in coal, 25 parts of water-containing sludges, 45 parts in water, 1 part of additive, 1 part of sludge modification medicament.
(2) preparation method
At first, placed 4 hours, obtain modified sewage sludge sewage sludge and sludge modification medicament thorough mixing.With modified sewage sludge, coal, water and additive ground and mixed, make high concentration sludge coal slurry then
3. product performance index
(1) face shaping------grey black slurry.Under 25 ℃, apparent viscosity has good flowability below 1000mPas, but pumping
(2) solid holdup (weight %)------60
(3) in the slurry solid grain size less than (millimeter)------0.5
4. end-use
The place of water coal slurry, act as a fuel be used for 20 tons/time coal water slurry boiler.The fuel burnout rate can reach more than 98%, is sparing in the use of coal 3%.
Embodiment 2
1. raw material
(1) sewage sludge of Shanghai City sewage work generation, water-content------80%, weight;
(2) certain colliery lump coal, water-content------2%, ash content------8%;
(3) additive (methyl naphthalene sulfonate formaldehyde condensate)
(4) sludge modification medicament (calcium hydroxide)
(5) tap water
2. preparation condition
(1) proportioning raw materials (parts by weight)
150 parts in coal, 45 parts of water-containing sludges, 58 parts in water, 1.5 parts of additives, 1 part of sludge modification medicament.
(2) preparation method
At first, placed 3 days, obtain modified sewage sludge sewage sludge and sludge modification medicament thorough mixing.With modified sewage sludge, coal, water and additive ground and mixed, make high concentration sludge coal slurry then
3. product performance index
(1) face shaping------grey black slurry.Under 25 ℃, apparent viscosity has good flowability below 1000mPas, but pumping.
(2) solid holdup (weight %)------61
(3) in the slurry solid grain size less than (millimeter)------0.5
4. end-use
The place of water coal slurry is used for preparing synthetic gas as patent 98110616.1 described multi-nozzle opposed type coal slurry gasifiers, effectively pneumatolytic branch (CO+H
2) can reach more than 80%, effectively the gas productive rate is 1.80Nm
3/ kg, efficiency of carbon conversion are sparing in the use of coal 4% more than 99%.
Claims (8)
1. a high concentration sludge coal slurry is characterized in that, component and parts by weight content comprise:
100～200 parts of coal dusts
10～50 parts of water-containing sludges
10～100 parts in water
1～5 part of additive
1～5 part of sludge modification medicament.
2. high concentration sludge coal slurry according to claim 1 is characterized in that, in the said water-containing sludge, water ratio is 50～95%, weight.
3. high concentration sludge coal slurry according to claim 1 is characterized in that, described coal is selected from brown coal, bituminous coal, hard coal or its mixture.
4. high concentration sludge coal slurry according to claim 2, it is characterized in that described water-containing sludge is selected from the sewage sludge of municipal sewage plant's generation, wastewater sludge, the paper mill effluent that Industrial Wastewater Treatment produces handled paper mill sludge or its mixture that produces.
5. high concentration sludge coal slurry according to claim 1 is characterized in that, additive is any one or a few in naphthalenesulfonate, polycarboxylate or the sulfonated lignin.
6. high concentration sludge coal slurry according to claim 1 is characterized in that, the sludge modification medicament is any one or a few in lime carbonate, yellow soda ash, sodium bicarbonate, salt of wormwood, calcium hydroxide, sodium hydroxide or the potassium hydroxide.
7. according to the preparation method of each described high concentration sludge coal slurry of claim 1～6, it is characterized in that, comprise the steps:
Water-containing sludge is mixed with the sludge modification medicament, obtain the modification water-containing sludge, preferably mix the back and placed 2～240 hours;
Then above-mentioned modification water-containing sludge, coal dust, water and additive are mixed, grind, the particle diameter that makes solid particulate promptly obtains said high concentration sludge coal slurry less than 0.5mm.
8. according to the application of each described high concentration sludge coal slurry of claim 1～6, it is characterized in that, as boiler oil or vaporising fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610030071 CN1908134A (en) | 2006-08-14 | 2006-08-14 | High concentration sludge coal slurry and method for preparing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610030071 CN1908134A (en) | 2006-08-14 | 2006-08-14 | High concentration sludge coal slurry and method for preparing the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1908134A true CN1908134A (en) | 2007-02-07 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200610030071 Pending CN1908134A (en) | 2006-08-14 | 2006-08-14 | High concentration sludge coal slurry and method for preparing the same |
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| Country | Link |
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| CN (1) | CN1908134A (en) |
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101747942A (en) * | 2009-12-30 | 2010-06-23 | 昆明理工大学 | Oxygen-enriched melting gasification method for lake sediment and device therefor |
| CN101054541B (en) * | 2007-04-26 | 2010-11-24 | 华东理工大学 | A kind of sludge petroleum coke slurry and its preparation method and application |
| CN101985572A (en) * | 2010-11-25 | 2011-03-16 | 东南大学 | High-concentration sludge coke slurry and preparation method thereof |
| CN102041100A (en) * | 2009-10-10 | 2011-05-04 | 华东理工大学 | Method for treating high-concentration organic wastewater |
| CN102191085A (en) * | 2010-03-04 | 2011-09-21 | 北京中矿环保科技股份有限公司 | Method for using sludge to produce coal gas |
| CN102311809A (en) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | Method for producing synthesis gas from oil sludge |
| CN102557361A (en) * | 2010-12-23 | 2012-07-11 | 新奥科技发展有限公司 | Sludge gasification method |
| CN102732345A (en) * | 2012-07-10 | 2012-10-17 | 煤炭科学研究总院 | Sludge coal-water slurry and preparation method thereof |
| CN102977954A (en) * | 2012-12-10 | 2013-03-20 | 贵州金赤化工有限责任公司 | Low-ash fusion point anthracitic water-coal slurry for coal gasification and preparation method thereof |
| CN103013613A (en) * | 2012-12-24 | 2013-04-03 | 西安科技大学 | Clean fuelization system and fuelization method for urban sludge |
| CN103468333A (en) * | 2012-06-06 | 2013-12-25 | 中国石油天然气股份有限公司 | Oily sludge coke water slurry and preparation method thereof |
| CN103497791A (en) * | 2013-09-18 | 2014-01-08 | 煤炭科学研究总院 | Novel sludge coal-water slurry and preparation method thereof |
| CN103540374A (en) * | 2012-07-09 | 2014-01-29 | 王庆 | Modified sludge coal slurry and preparation method thereof |
| CN104479794A (en) * | 2014-10-24 | 2015-04-01 | 东方电气集团东方锅炉股份有限公司 | Flux for reducing fine coal gasification ash melting point temperature and use method thereof |
| CN104479793A (en) * | 2014-10-24 | 2015-04-01 | 东方电气集团东方锅炉股份有限公司 | Composite flux for reducing fine coal gasification ash melting point temperature |
| CN106475393A (en) * | 2015-08-27 | 2017-03-08 | 中国石油化工股份有限公司 | A kind of harmless treatment method of acetic acid residue |
| CN107164004A (en) * | 2017-04-21 | 2017-09-15 | 华北电力大学（保定） | A kind of utilization alkaline matter breaking sludge floc sedimentation promotes sludge water-coal-slurry into the method for slurry |
| CN108949267A (en) * | 2018-08-02 | 2018-12-07 | 中煤科工清洁能源股份有限公司 | A kind of high concentration sludge coal slurry, preparation method and the usage |
| US10287522B2 (en) | 2013-01-31 | 2019-05-14 | General Electric Company | System and method for preparing coal water slurry |
| CN109775952A (en) * | 2019-04-03 | 2019-05-21 | 广州绿邦环境技术有限公司 | A kind of Processes and apparatus that recycling sludge utilizes |
| CN110628480A (en) * | 2019-10-14 | 2019-12-31 | 宋合富 | Method for preparing combustible sludge through municipal sludge and fire coal |
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2006
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Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101054541B (en) * | 2007-04-26 | 2010-11-24 | 华东理工大学 | A kind of sludge petroleum coke slurry and its preparation method and application |
| CN102041100A (en) * | 2009-10-10 | 2011-05-04 | 华东理工大学 | Method for treating high-concentration organic wastewater |
| CN101747942A (en) * | 2009-12-30 | 2010-06-23 | 昆明理工大学 | Oxygen-enriched melting gasification method for lake sediment and device therefor |
| CN102191085A (en) * | 2010-03-04 | 2011-09-21 | 北京中矿环保科技股份有限公司 | Method for using sludge to produce coal gas |
| CN102311809A (en) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | Method for producing synthesis gas from oil sludge |
| CN102311809B (en) * | 2010-07-07 | 2016-04-13 | 中国石油化工股份有限公司 | Method for producing synthesis gas by using oil sludge as raw material |
| CN101985572A (en) * | 2010-11-25 | 2011-03-16 | 东南大学 | High-concentration sludge coke slurry and preparation method thereof |
| CN102557361A (en) * | 2010-12-23 | 2012-07-11 | 新奥科技发展有限公司 | Sludge gasification method |
| CN102557361B (en) * | 2010-12-23 | 2015-01-07 | 新奥科技发展有限公司 | Sludge gasification method |
| CN103468333A (en) * | 2012-06-06 | 2013-12-25 | 中国石油天然气股份有限公司 | Oily sludge coke water slurry and preparation method thereof |
| CN103540374A (en) * | 2012-07-09 | 2014-01-29 | 王庆 | Modified sludge coal slurry and preparation method thereof |
| CN103540374B (en) * | 2012-07-09 | 2017-12-22 | 任相坤 | A kind of modified sewage sludge coal slurry and preparation method thereof |
| CN102732345A (en) * | 2012-07-10 | 2012-10-17 | 煤炭科学研究总院 | Sludge coal-water slurry and preparation method thereof |
| CN102732345B (en) * | 2012-07-10 | 2014-09-10 | 煤炭科学研究总院 | Sludge coal-water slurry and preparation method thereof |
| CN102977954A (en) * | 2012-12-10 | 2013-03-20 | 贵州金赤化工有限责任公司 | Low-ash fusion point anthracitic water-coal slurry for coal gasification and preparation method thereof |
| CN103013613A (en) * | 2012-12-24 | 2013-04-03 | 西安科技大学 | Clean fuelization system and fuelization method for urban sludge |
| US10287522B2 (en) | 2013-01-31 | 2019-05-14 | General Electric Company | System and method for preparing coal water slurry |
| CN103497791A (en) * | 2013-09-18 | 2014-01-08 | 煤炭科学研究总院 | Novel sludge coal-water slurry and preparation method thereof |
| CN104479794A (en) * | 2014-10-24 | 2015-04-01 | 东方电气集团东方锅炉股份有限公司 | Flux for reducing fine coal gasification ash melting point temperature and use method thereof |
| CN104479793A (en) * | 2014-10-24 | 2015-04-01 | 东方电气集团东方锅炉股份有限公司 | Composite flux for reducing fine coal gasification ash melting point temperature |
| CN104479794B (en) * | 2014-10-24 | 2016-03-30 | 东方电气集团东方锅炉股份有限公司 | A kind of fusing assistant and using method thereof reducing gasified pulverized coal slag ash fusion point temperature |
| CN104479793B (en) * | 2014-10-24 | 2016-03-30 | 东方电气集团东方锅炉股份有限公司 | A kind of composite fluxing agent reducing gasified pulverized coal slag ash fusion point temperature |
| CN106475393A (en) * | 2015-08-27 | 2017-03-08 | 中国石油化工股份有限公司 | A kind of harmless treatment method of acetic acid residue |
| CN107164004A (en) * | 2017-04-21 | 2017-09-15 | 华北电力大学（保定） | A kind of utilization alkaline matter breaking sludge floc sedimentation promotes sludge water-coal-slurry into the method for slurry |
| CN108949267A (en) * | 2018-08-02 | 2018-12-07 | 中煤科工清洁能源股份有限公司 | A kind of high concentration sludge coal slurry, preparation method and the usage |
| CN108949267B (en) * | 2018-08-02 | 2021-02-02 | 中煤科工清洁能源股份有限公司 | High-concentration sludge coal slurry, preparation method and application thereof |
| CN109775952A (en) * | 2019-04-03 | 2019-05-21 | 广州绿邦环境技术有限公司 | A kind of Processes and apparatus that recycling sludge utilizes |
| CN109775952B (en) * | 2019-04-03 | 2021-11-26 | 广州绿邦环境技术有限公司 | Process and equipment for resource utilization of sludge |
| CN110628480A (en) * | 2019-10-14 | 2019-12-31 | 宋合富 | Method for preparing combustible sludge through municipal sludge and fire coal |
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