CN108165331A - A kind of Compositional type slurries additive agent - Google Patents

A kind of Compositional type slurries additive agent Download PDF

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Publication number
CN108165331A
CN108165331A CN201810128578.3A CN201810128578A CN108165331A CN 108165331 A CN108165331 A CN 108165331A CN 201810128578 A CN201810128578 A CN 201810128578A CN 108165331 A CN108165331 A CN 108165331A
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additive agent
slurries additive
coal
sodium
phosphate
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辛志国
王立静
张兰翔
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Dezhou Dehua Chemical Industry Co Ltd
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Dezhou Dehua Chemical Industry Co Ltd
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Priority to CN201810128578.3A priority Critical patent/CN108165331A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1233Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1266Inorganic compounds nitrogen containing compounds, (e.g. NH3)
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1283Inorganic compounds phosphorus, arsenicum, antimonium containing compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1988Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid epoxy resins and derivatives; natural resins, e.g. colophony
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/236Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
    • C10L1/2364Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof homo- or copolymers derived from unsaturated compounds containing amide and/or imide groups
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • C10L1/2437Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2462Organic compounds containing sulfur, selenium and/or tellurium macromolecular compounds

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)

Abstract

The invention discloses a kind of cheap, efficient, cost-effective Compositional type slurries additive agents.Each component weight proportion relation is:10%~30% naphthalene sulphonate formaldehyde polymer, 70%~80% lignosulfonates, 1%~10% acid-base modifier, 0.01 ‰~0.05 ‰ polyolefin, 0.01 ‰~0.05 ‰ polyethylene oxide, 0.001 ‰~0.003 ‰ polyethers, 1%~3% phosphate.Above-mentioned each component by proportioning in the form of pulvis or aqueous solution is mixed evenly, the aqueous solution of solid-state pulverulent mixture or mass fraction≤40% is made, then adds in slurrying in coal-water mixture, butt dosage is 0.5 ‰~1.5 ‰.Water-coal-slurry slurry concentration prepared by the present invention is high, viscosity is low, mobility is good, stability is good, coal adaptability is strong.

Description

A kind of Compositional type slurries additive agent
Technical field
The present invention relates to coal gasification commercial Application, in particular to a kind of cheap, efficient, cost-effective Compositional type Slurries additive agent.
Background technology
China is the country of the rich few oil of coal, and rich coal resources account for about the 70% of domestic energy consumption.The biography of coal Application method lime-ash of uniting is more, pollution is big, transport difficult and expensive, burning and heating efficiency be not high.Water-coal-slurry is a kind of use The environmental clean fuel of New type coal base flow body and a kind of coal prepared by physical method does the novel original of raw material production synthesis gas Material.The technology passes through to coal resources deep processing, rationally using improving the utilization rate of coal resources.
In water-coal-slurry raw material production cost, other than 60%~70% coal and 30%~40% water, water-coal-slurry is improved The slurries additive agent of performance constitutes the second largest cost factor of water-coal-slurry.Slurries additive agent is to the viscosity of water-coal-slurry, dense The key indexes such as degree, stability and mobility suffer from directly influencing, so, reduce the use of slurries additive agent into This, improving effective utilization becomes a key subject of current COAL-WATER SLURRY TECHNOLOGY.
At present, domestic and international slurries additive agent is broadly divided into two major class of anionic and neutral ionic.By its chemical group Into difference, be divided into for:Naphthalenesulfonate formaldehyde condensation compound, lignosulfonates, humate, polycarboxylic acids, polyolefin, aliphatic poly Close object, polyethers and long-chain alcohol ketone derivatives etc..
Different slurries additive agents disperses viscosity reduction ability, slurry concentration, mobility and stability to same coal Effect is different.All in all, anionic slurries additive agent-naphthalenesulfonate formaldehyde condensation compound that the country largely uses at present Its dispersion performance, slurry mobility are preferable, applied widely, however slurry stability is poor, and due to producing naphthalene sulfonate The higher price of raw material-naphthalene of formaldehyde condensation products, the cost price for leading to naphthalenesulfonate formaldehyde condensation compound is higher, a large amount of to use Cause production cost higher so that the slurries additive agent competitiveness of naphthalenesulfonate formaldehyde condensation compound class declines.Lignin sulfonic acid For salt compared with naphthalenesulfonate formaldehyde condensation compound, price advantage is apparent, and raw material resources are enriched and are easy to get, and slurrying stability compared with It is good.But the complicated component and performance due to the lignin as raw materials for production are unstable, lignosulfonates it is slurry Performance is also unstable, it is difficult to meet commercial Application requirement.Humate is extracted from low price coal, and dispersion performance is preferable, but It easily forms precipitation, the stability of slurry is very poor to metal ion-sensitive.Polycarboxylic acids, aliphatic polymer, gathers polyolefin Ethers and long-chain alcohol ketone derivatives are according to the difference of its molecular weight, and using effect is different, and all in all, effect is better than Naphthalenesulfonate formaldehyde condensation compound, lignosulfonates and humate, but due to strictly to control molecular weight and at high price, It cannot be widely used to promote.
China's slurries additive agent type currently in use is various at present, and quality is irregular, cost performance it is not high or Efficiently at high price or cheap performance is bad, it is difficult to meet increasingly competitive industrialization development.In addition, with environmental protection Pressure increases, often with the buck of gasification system, steam condensate (SC), other process units during coal water slurry gasifying device slurrying It produces one or more of waste water, biochemical water, alkali waste water etc. and partly or entirely replaces technique desalted water, considerably increase water coal The slurrying difficulty of slurry.The slurries additive agent of single use a certain kind component can not meet the development of coal water slurry gasifying device It is required that therefore, we must develop a kind of higher high ecad Compositional type slurries additive agent of sexual valence, to cope with water-coal-slurry The increasingly complicated operating mode of gasification installation pulping system, improves water coal slurry concentration, reduces viscosity of coal slurry, improve water-coal-slurry mobility, Expand gasification slurrying coal range.
Invention content
The present invention provides a kind of commercial Application performance and stablizes, coal is applied widely, and valency using the method for compounding The cheap high performance-price ratio slurries additive agent of lattice.
A kind of technical solution of the present invention is to form water-coal-slurry using the mixture of certain formula rate to add Agent, concrete component and mass percent are:
Naphthalene sulphonate formaldehyde polymer 10%~30%
Lignosulfonates 70%~80%
Acid-base modifier 1%~10%
Polyolefin 0.01 ‰~0.05 ‰
Polyethylene oxide 0.01 ‰~0.05 ‰
Polyethers 0.001 ‰~0.003 ‰
Phosphate 1%~3%
The naphthalene sulphonate formaldehyde polymer is selected from β-naphthalene sulfonate formaldehyde polymer, methanonaphthalene sodium sulfonate oxymethylene polymerization Object, α-naphthalenesulfonicacid sodium formaldehyde polymer or one kind or any two combination of the above in benzyl benzene sulfonic acid sodium salt yuban.
The one kind of the lignosulfonates in sodium lignin sulfonate, calcium lignosulfonate or ammonium lignosulphonate Or any two combination of the above.
One kind in sodium hydroxide, potassium hydroxide, ammonium hydroxide or phosphoric acid of the acid-base modifier or any two more than Combination.
The one kind or any two combination of the above of the polyolefin in polyvinyl lactam or polyacrylamide.
The polyethylene oxide is selected from one or both of polyethylene glycol PEG or polyethylene glycol oxide PEO combination.
The polyethers are selected from ethoxylated dodecyl alcohol, alkyl phenol polyoxyethylene ether or D-sorbite polyoxyethylene ether In one kind or any two combination of the above.
The one kind or wantonly two of the phosphate in tertiary sodium phosphate, ammonium phosphate, sodium tripolyphosphate or potassium tripolyphosphate Kind combination of the above.
Above-mentioned each component is mixed evenly the present invention by proportioning in the form of pulvis or aqueous solution, and solid-state powdery is made Then the aqueous solution of mixture or mass fraction≤40% adds in slurrying in coal-water mixture.
The present invention requirement of performances such as is particularly suitable for disperseing during water-coal-slurry slurring, stablize, being real by constantly improvement One of optimal slurries additive agent of existing water-coal-slurry storage, pumping, atomization, stable burning etc..
Additive amount of the present invention is depending on coal quality and operating mode, it is proposed that dosage is 0.5 ‰~the 1.5 ‰ of coal dust butt proportion.
Specific embodiment
In order to which those skilled in the art is made to more fully understand the present invention, specific embodiment below is made the present invention into one Step is described in detail.
A kind of Compositional type slurries additive agent is prepared, component and mass mixing percentage are as follows:
β-formaldehyde polysulfonate acid sodium formaldehyde polymer 19%:
Calcium lignosulfonate 78%:
Sodium hydroxide 1%:
Acrylamide 0.02 ‰:
Polyethylene glycol 0.03 ‰:
Ethoxylated dodecyl alcohol 0.001 ‰
Tertiary sodium phosphate 1.949%.
It is uniformly mixed according to the above ratio, prepares Compositional type slurries additive agent
Embodiment 1:
The coal sample place of production:Even tower ore deposit point is mended by Shenhua
By weight percentage by butt coal 62%, water 37.89%, the mixing of slurries additive agent butt dosage 1 ‰ of the present invention, use Blender is stirred evenly after ten minutes to get to concentration 62% or so, viscosity 550mPa.s, density 1.19g/cm3, mobility 8~ 10s, stability 0.5%, the water-coal-slurry of pH value 8~9.
Example 2:
The coal sample place of production:Shenhua porcelain kiln gulf ore deposit point
By weight percentage by butt coal 62%, water 37.89%, the mixing of slurries additive agent butt dosage 1 ‰ of the present invention, use Blender is stirred evenly after ten minutes to get to concentration 62% or so, viscosity 610mPa.s, density 1.19g/cm3, mobility 8~ 10s, stability 0.5%, the water-coal-slurry of pH value 8~9.
Example 3:
The coal sample place of production:Shenhua Huan County ore deposit point
By weight percentage by butt coal 62%, water 37.89%, additive of the present invention butt dosage 1 ‰ mixes, and uses blender It stirs evenly after ten minutes to get to concentration 62% or so, viscosity 570mPa.s, density 1.19g/cm3, 8~10s of mobility, surely Qualitative 0.5%, the water-coal-slurry of pH value 8~9.
Example 4:
The coal sample place of production:Ore deposit point in gulf in Shenhua
By weight percentage by butt coal 62%, water 37.89%, additive of the present invention butt dosage 1 ‰ mixes, and uses blender It stirs evenly after ten minutes to get to concentration 62% or so, viscosity 630mPa.s, density 1.19g/cm3, 8~10s of mobility, surely Qualitative 0.5%, the water-coal-slurry of pH value 8~9.
Example 5:
The coal sample place of production:The red valley ore deposit point of Shenhua
By weight percentage by butt coal 62%, water 37.89%, additive of the present invention butt dosage 1 ‰ mixes, and uses blender It stirs evenly after ten minutes to get to concentration 62% or so, viscosity 530mPa.s, density 1.19g/cm3, 8~10s of mobility, surely Qualitative 0.5%, the water-coal-slurry of pH value 8~9.Preferably supplement
From examples detailed above as can be seen that finished product water coal slurry concentration height prepared by additive of the present invention, can stably reach 62%, add Dosage is low, and additive butt additive amount is 0.5 ‰~1.5 ‰, and viscosity is low, and mobility, stability are preferable, coal adaptability By force.
Additive of the present invention can be configured to aqueous solution of the concentration below 40%, be added to rod mill, ball milling in the form of a solution In machine or agitator, solid powder mixture can also be prepared into, is added in grinding machine with powdery, is applied in commercial plant Effect is more apparent, is particularly suitable for wet method pulping process.
Various embodiments of the present invention are described above, above description is exemplary, and non-exclusive, and It is not limited to disclosed each embodiment.In the case of without departing from the scope and spirit of illustrated each embodiment, for this skill Many modifications and changes will be apparent from for the those of ordinary skill in art field.Therefore, protection scope of the present invention should This is subject to the protection scope in claims.

Claims (9)

1. a kind of slurries additive agent, component and mass percent are as follows:
Naphthalene sulphonate formaldehyde polymer 10%~30%
Lignosulfonates 70%~80%
Acid-base modifier 1%~10%
Polyolefin 0.01 ‰~0.05 ‰
Polyethylene oxide 0.01 ‰~0.05 ‰
Polyethers 0.001 ‰~0.003 ‰
Phosphate 1%~3%.
2. invention slurries additive agent according to claim 1, which is characterized in that the naphthalene sulphonate formaldehyde polymer Selected from β-naphthalene sulfonate formaldehyde polymer, methanonaphthalene sodium sulfonate yuban, α-naphthalenesulfonicacid sodium formaldehyde polymer or benzyl At least one of benzene sulfonic acid sodium salt yuban.
3. invention slurries additive agent according to claim 1, which is characterized in that the lignosulfonates are selected from wood At least one of quality sodium sulfonate, calcium lignosulfonate or ammonium lignosulphonate.
4. invention slurries additive agent according to claim 1, which is characterized in that the acid-base modifier is selected from hydrogen-oxygen Change at least one of sodium, potassium hydroxide, ammonium hydroxide or phosphoric acid.
5. invention slurries additive agent according to claim 1, which is characterized in that the polyolefin is selected from polyethylene At least one of amide or polyacrylamide.
6. invention slurries additive agent according to claim 1, which is characterized in that the polyethylene oxide is selected from poly- second At least one of glycol or polyethylene glycol oxide.
7. invention slurries additive agent according to claim 1, which is characterized in that the polyethers are gathered selected from laruyl alcohol At least one of ethylene oxide ether, alkyl phenol polyoxyethylene ether or D-sorbite polyoxyethylene ether.
8. invention slurries additive agent according to claim 1, which is characterized in that the phosphate is selected from tricresyl phosphate At least one of sodium, ammonium phosphate, sodium tripolyphosphate or potassium tripolyphosphate.
9. a kind of application method of slurries additive agent, the component and mass percent of the slurries additive agent are as follows:
Naphthalene sulphonate formaldehyde polymer 10%~30%
Lignosulfonates 70%~80%
Acid-base modifier 1%~10%
Polyolefin 0.01 ‰~0.05 ‰
Polyethylene oxide 0.01 ‰~0.05 ‰
Polyethers 0.001 ‰~0.003 ‰
Phosphate 1%~3%
First, according to above-mentioned each component and its proportioning physical mixed be prepared slurries additive agent solid powder or will more The component aqueous solution soluble in water that slurries additive agent mass percent≤40% is prepared in proportion;
Then, the aqueous solution of the solid powder of the slurries additive agent or slurries additive agent is added in butt coal dust, It stirs evenly, slurrying;
The dosage of the slurries additive agent is 0.5 ‰~the 1.5 ‰ of butt coal dust weight.
CN201810128578.3A 2018-02-08 2018-02-08 A kind of Compositional type slurries additive agent Pending CN108165331A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109161417A (en) * 2018-11-16 2019-01-08 山东正祎环保科技有限公司 A kind of neutrality slurries additive agent and its application
CN109536224A (en) * 2018-12-29 2019-03-29 广东汇昇环保科技有限公司 Water-coal-slurry, preparation method and the application method of dangerous waste coal-tar residue production
CN111534344A (en) * 2020-05-29 2020-08-14 新沂市建科新材料有限公司 Preparation method of lignin additive
CN112625765A (en) * 2020-11-09 2021-04-09 山东格瑞兰德添加剂有限公司 CMN type coal water slurry additive

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103509617A (en) * 2013-01-17 2014-01-15 湖南东盈煤化工技术开发有限公司 Special composite coal water slurry additive for coal gasification

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103509617A (en) * 2013-01-17 2014-01-15 湖南东盈煤化工技术开发有限公司 Special composite coal water slurry additive for coal gasification

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陈清如等: "《中国洁净煤技术》", 30 September 2009, 中国矿业大学出版社 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109161417A (en) * 2018-11-16 2019-01-08 山东正祎环保科技有限公司 A kind of neutrality slurries additive agent and its application
CN109536224A (en) * 2018-12-29 2019-03-29 广东汇昇环保科技有限公司 Water-coal-slurry, preparation method and the application method of dangerous waste coal-tar residue production
CN111534344A (en) * 2020-05-29 2020-08-14 新沂市建科新材料有限公司 Preparation method of lignin additive
CN112625765A (en) * 2020-11-09 2021-04-09 山东格瑞兰德添加剂有限公司 CMN type coal water slurry additive

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Application publication date: 20180615