CN108531231A - A kind of preparation method of low metal responsive type coal water slurry dispersing agent - Google Patents

A kind of preparation method of low metal responsive type coal water slurry dispersing agent Download PDF

Info

Publication number
CN108531231A
CN108531231A CN201810372355.1A CN201810372355A CN108531231A CN 108531231 A CN108531231 A CN 108531231A CN 201810372355 A CN201810372355 A CN 201810372355A CN 108531231 A CN108531231 A CN 108531231A
Authority
CN
China
Prior art keywords
coal
parts
dispersing agent
water slurry
slurry dispersing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
CN201810372355.1A
Other languages
Chinese (zh)
Inventor
林正脉
蒋益
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Changzhou Five Glory Chemical Co Ltd
Original Assignee
Changzhou Five Glory Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Changzhou Five Glory Chemical Co Ltd filed Critical Changzhou Five Glory Chemical Co Ltd
Priority to CN201810372355.1A priority Critical patent/CN108531231A/en
Publication of CN108531231A publication Critical patent/CN108531231A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • C10L1/32Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/326Coal-water suspensions
    • 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
    • C10L1/106Liquid carbonaceous fuels containing additives mixtures of inorganic compounds with organic macromolecular 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/18Use of additives to fuels or fires for particular purposes use of detergents or dispersants for purposes not provided for in groups C10L10/02 - C10L10/16
    • 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
    • C10L1/1225Inorganic compounds halogen 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
    • C10L1/12Inorganic compounds
    • C10L1/1233Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
    • C10L1/125Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
    • 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
    • C10L1/1275Inorganic compounds sulfur, tellurium, selenium 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
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
    • 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
    • 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
    • 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
    • C10L1/28Organic compounds containing silicon
    • 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
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/305Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond)

Landscapes

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

Abstract

The present invention relates to a kind of preparation methods of low metal responsive type coal water slurry dispersing agent, belong to coal mine field of material technology.Technical solution of the present invention prepares humic acid and modified coal water slurry dispersing agent using potassium humate, due to a large amount of negative electrical charges of coal grain surface hydrophilic region band, when effective dispersant agent molecule is in coal grain adsorption, coal water slurry dispersing agent can not only be closed by hydrophobic effect in coal burl, Cationic functional groups on its strand can also be strongly adsorbed in by electrostatic force on coal grain surface, aligning more closely can be formed on coal grain surface, improve coal grain surface hydrophilicity, coal grain is separated by means of hydration shell, to reduce the viscosity of water-coal-slurry, improve the dispersion performance of coal water slurry dispersing agent.

Description

A kind of preparation method of low metal responsive type coal water slurry dispersing agent
Technical field
The present invention relates to a kind of preparation methods of low metal responsive type coal water slurry dispersing agent, belong to coal mine material technology neck Domain.
Background technology
In the preparation process of water-coal-slurry, add a small amount of dispersant can play the role of it is vital.Dispersant can By changing coal particle surface property, can be homogeneously dispersed in slurry, to make water-coal-slurry with lower apparent Viscosity and good rheological characteristic.Its mechanism of action can be illustrated by following three aspects:
For the effect of 1 wetting and dispersing since coal is mainly a kind of nonpolar hydrocarbon, surface has strong hydrophobicity.This Outside, since the surface tension of water is more much larger than coal surface tension, two aspect factors, which combine, causes coal grain cannot It is fully soaked, can not be uniformly dispersed.Dispersant molecule hydrophobic effect by hydrophobic side and coal grain surface in conjunction in a manner of and It is adsorbed on coal grain surface, water-wet side is then aligned and combined with water, is turned hydrophobic to be hydrophilic, is formed simultaneously one layer of hydration shell. The hydration shell can be effectively reduced coal-water interfacial tension, and coal grain is separated, to reduce the viscosity of water-coal-slurry.
2 electrostatic repulsion dehesions effect dlvo theory thinks, the Van der Waals force between charged colloidal particle and electrostatic repulsion it Between magnitude relationship determine its can stable dispersion, if Van der Waals force be less than electrostatic repulsion if it is colloid-stabilised, otherwise it is unstable. There are a variety of oxygen-containing functional groups such as hydroxyl, carboxyl on coal surface, and dissociation is so that coal shows elecrtonegativity, Zeta potential one in water As be -15~-20mv.Anionic dispersing agent, which is adsorbed on coal grain surface, can effectively enhance its electrostatic repulsion, promote coal grain It is better dispersed in water.
3 steric hindrance dehesion effects are hydrophilic in molecule when dispersant adsorption is aligned in coal particle surface presentation End can form one layer of three-dimensional hydration shell on coal surface.When coal particle is moved close to each other, hydration shell, which is squeezed, to be deformed, and is passed through Mechanical elasticity promotes coal grain is evenly dispersed to come.In addition, dispersant itself, which is formed by adsorption layer, has certain thickness, when two Close to when squeezing, the free movement of the molecule in adsorption layer is affected complex coal particle, reduces the entropy of coal slurry system. Chemical thermodynamics thinks that the entropy of isolated blob is carried out towards the direction of growth always.So promoting that extrusion cladding coal grain occurs again It is secondary separated, cause the dispersion of coal grain to suspend.
The water-coal-slurry for reaching commercial Application demand need to have high concentration, low apparent viscosity and outstanding rheological characteristic, stabilization The performance characteristics such as property.In the preparation process of water-coal-slurry, adds a small amount of dispersant and extremely key is played to the performance of water-coal-slurry Effect.Currently, what is be most widely used in the market is naphthalene sulfonate system dispersant, although such dispersant has good point Dissipate performance, excellent dehesion effect and it is applied widely the advantages that, but its slurrying stability is poor.China's humic acid resource is extremely Abundant, humic acid system coal water slurry dispersing agent is primarily referred to as humate and its modified product, its main feature is that raw material be easy to get it is inexpensive, and The problems such as slurrying favorable dispersibility, can be used alone, but that equally there is also slurry stabilities is poor, more sensitive to metal ion. Therefore how in the case where ensuring good dehesion effect, the emphasis that stability is existing coal water slurry dispersing agent research is improved.
Invention content
The technical problems to be solved by the invention:It is poor for existing coal water slurry dispersing agent stability of material, to metal ion Sensitive issue provides a kind of preparation method of low metal responsive type coal water slurry dispersing agent.
In order to solve the above technical problems, the technical solution adopted by the present invention is:
(1)In mass ratio 1:8, corrosive acid potassium is added in hydrochloric acid solution, stirs mixed rear and stands, filter and collect filter residue, Washing, drying, grind to obtain modified particles;Nitrogen is passed through to absolute ethyl alcohol, leads to nitrogen treatment, obtains modification liquid;
(2)Count in parts by weight, respectively weigh 45~50 parts of modification liquids, 10~15 parts of deionized waters, 25~30 parts of absolute ethyl alcohols, 10~15 parts of tetraethoxysilanes are placed in three-necked flask, and insulation reaction obtains mixed liquor and by volume 1:8, by γ-aminopropyl Tetraethoxysilane is added dropwise in mixed liquor, and after being added dropwise to complete, heating in water bath for reaction collects to obtain reaction solution;
(3)It places reaction liquid into dialysis membrane, dialysed using absolute ethyl alcohol and collects dialysis modification liquid, in mass ratio 1:5, by alkene Propyl sulfonic acid sodium is stirred and adjusts pH to 9.0 with dodecyl trimethyl ammonium chloride, obtains matrix liquid;
(4)It counts in parts by weight, weighs 45~50 parts of matrix liquid, 10~15 parts of dialysis modification liquids, 15~20 parts of modifications respectively Grain and 3~5 parts of polyvinyl alcohol are placed in beaker, are stirred and are adjusted pH to 9.0, obtain modified mixed liquor;
(5)Modified mixed liquor is placed in three-necked flask, at 75~85 DEG C, in mass ratio 1:15, ammonium persulfate solution is dripped It adds in modified mixed liquor, after being added dropwise to complete, insulation reaction, standing is cooled to room temperature, ultrasonic disperse, you can be prepared into described Low metal responsive type coal water slurry dispersing agent.
Step(1)It is 25~30mL/min that the nitrogen, which is passed through rate,.
Step(2)The γ-aminopropyl tetraethoxysilane drop rate is 2~3mL/min.
Compared with other methods, advantageous effects are the present invention:
(1)Technical solution of the present invention there is excellent sensitive property to change metal ion by modifying silicon Nano sol and preparing Property agent, technical solution of the present invention adequately adsorbs metal ion by the sensitive decorative layer on Ludox surface, to have Effect reduces jamming performance of the metal ion to the metal ion of effective dispersant agent material, to improve in technical solution of the present invention The stability of coal water slurry dispersing agent;
(2)Technical solution of the present invention prepares humic acid and modified coal water slurry dispersing agent using potassium humate, due to coal grain surface parent The a large amount of negative electrical charges of water area band, when effective dispersant agent molecule is in coal grain adsorption, coal water slurry dispersing agent can not only lead to It crosses hydrophobic effect to close in coal burl, the Cationic functional groups on strand can also be strongly adsorbed in by electrostatic force On coal grain surface, aligning more closely can be formed on coal grain surface, improve coal grain surface hydrophilicity, borrow hydration shell will Coal grain separates, and to reduce the viscosity of water-coal-slurry, improves the dispersion performance of coal water slurry dispersing agent.
Specific implementation mode
In mass ratio 1:8, corrosive acid potassium is added in 1% hydrochloric acid solution of mass fraction, stir it is mixed after and stand 20~ For 24 hours, filter residue is filtered and collects, it is 7.0 to be rinsed to cleaning solution pH with deionized water, then dry 3~5h at 75~80 DEG C, grinding Obtain modified particles;Nitrogen is passed through to absolute ethyl alcohol, it is 25~30mL/min that control nitrogen, which is passed through rate, nitrogen to be led to 25~ 30min obtains modification liquid, then counts in parts by weight, weighs 45~50 parts of modification liquids, 10~15 parts of deionized waters, 25~30 respectively Part absolute ethyl alcohol, 10~15 parts of tetraethoxysilanes are placed in three-necked flask, at 45~50 DEG C after 3~5h of insulation reaction, are obtained Mixed liquor and by volume 1:8, γ-aminopropyl tetraethoxysilane is added dropwise in mixed liquor, control drop rate be 2~ 3mL/min, after being added dropwise to complete, then at 75~85 DEG C react 10~12h, collect reaction solution is placed in dialysis membrane, adopt It is dialysed with absolute ethyl alcohol and collects dialysis modification liquid;In mass ratio 1:5, by Sodium Allyl Sulfonate and trimethyl chlorination Ammonium is stirred and 1% sodium hydroxide solution of mass fraction is used to adjust pH to 9.0, obtains matrix liquid and counts in parts by weight, respectively It weighs 45~50 parts of matrix liquid, 10~15 parts of dialysis modification liquids, 15~20 parts of modified particles and 3~5 parts of polyvinyl alcohol and is placed in burning It in cup, is stirred and adjusts pH to 9.0 with 1% sodium hydroxide solution of mass fraction, obtain modified mixed liquor, by modified mixed liquor It is placed in three-necked flask, at 75~85 DEG C, in mass ratio 1:15,1% ammonium persulfate solution of mass fraction is added dropwise to modification In mixed liquor, control ammonium persulfate drop rate is 2~3mL/min, after being added dropwise to complete, then the insulation reaction at 75~85 DEG C 3~5h, standing are cooled to room temperature, then 10~15min of ultrasonic disperse at 200~300W, you can are prepared into the low metal Responsive type coal water slurry dispersing agent.
Example 1
In mass ratio 1:8, corrosive acid potassium is added in 1% hydrochloric acid solution of mass fraction, stirs mixed rear and stands 20h, filter And filter residue is collected, it is 7.0 to be rinsed to cleaning solution pH with deionized water, then the dry 3h at 75 DEG C, grinds to obtain modified particles;To nothing Water-ethanol is passed through nitrogen, and it is 25mL/min that control nitrogen, which is passed through rate, and nitrogen 25min to be led to obtains modification liquid, then in parts by weight Meter weighs 45 parts of modification liquids, 10 parts of deionized waters, 25 parts of absolute ethyl alcohols, 10 parts of tetraethoxysilanes and is placed in three-necked flask respectively In, at 45 DEG C after insulation reaction 3h, obtain mixed liquor and by volume 1:8, γ-aminopropyl tetraethoxysilane is added dropwise to mixed It closes in liquid, control drop rate is 2mL/min, after being added dropwise to complete, then reacts 10h at 75 DEG C, collects to obtain reaction solution juxtaposition In dialysis membrane, is dialysed using absolute ethyl alcohol and collect dialysis modification liquid;In mass ratio 1:5, by Sodium Allyl Sulfonate and 12 Alkyl trimethyl ammonium chloride is stirred and 1% sodium hydroxide solution of mass fraction is used to adjust pH to 9.0, obtains matrix liquid and by weight Number meter is measured, 45 parts of matrix liquid, 10 parts of dialysis modification liquids, 15 parts of modified particles and 3 parts of polyvinyl alcohol is weighed respectively and is placed in beaker In, it is stirred and adjusts pH to 9.0 with 1% sodium hydroxide solution of mass fraction, obtain modified mixed liquor, modified mixed liquor is set In three-necked flask, at 75 DEG C, in mass ratio 1:15,1% ammonium persulfate solution of mass fraction is added dropwise to modified mixed liquor In, control ammonium persulfate drop rate is 2mL/min, and after being added dropwise to complete, then the insulation reaction 3h at 75 DEG C, standing are cooled to Room temperature, then the ultrasonic disperse 10min at 200W, you can be prepared into the low metal responsive type coal water slurry dispersing agent.
Example 2
In mass ratio 1:8, corrosive acid potassium is added in 1% hydrochloric acid solution of mass fraction, stirs mixed rear and stands 22h, filter And filter residue is collected, it is 7.0 to be rinsed to cleaning solution pH with deionized water, then the dry 4h at 77 DEG C, grinds to obtain modified particles;To nothing Water-ethanol is passed through nitrogen, and it is 27mL/min that control nitrogen, which is passed through rate, and nitrogen 27min to be led to obtains modification liquid, then in parts by weight Meter weighs 47 parts of modification liquids, 12 parts of deionized waters, 27 parts of absolute ethyl alcohols, 12 parts of tetraethoxysilanes and is placed in three-necked flask respectively In, at 47 DEG C after insulation reaction 4h, obtain mixed liquor and by volume 1:8, γ-aminopropyl tetraethoxysilane is added dropwise to mixed It closes in liquid, control drop rate is 2mL/min, after being added dropwise to complete, then reacts 11h at 80 DEG C, collects to obtain reaction solution juxtaposition In dialysis membrane, is dialysed using absolute ethyl alcohol and collect dialysis modification liquid;In mass ratio 1:5, by Sodium Allyl Sulfonate and 12 Alkyl trimethyl ammonium chloride is stirred and 1% sodium hydroxide solution of mass fraction is used to adjust pH to 9.0, obtains matrix liquid and by weight Number meter is measured, 47 parts of matrix liquid, 12 parts of dialysis modification liquids, 17 parts of modified particles and 4 parts of polyvinyl alcohol is weighed respectively and is placed in beaker In, it is stirred and adjusts pH to 9.0 with 1% sodium hydroxide solution of mass fraction, obtain modified mixed liquor, modified mixed liquor is set In three-necked flask, at 77 DEG C, in mass ratio 1:15,1% ammonium persulfate solution of mass fraction is added dropwise to modified mixed liquor In, control ammonium persulfate drop rate is 2mL/min, and after being added dropwise to complete, then the insulation reaction 4h at 80 DEG C, standing are cooled to Room temperature, then the ultrasonic disperse 12min at 250W, you can be prepared into the low metal responsive type coal water slurry dispersing agent.
Example 3
In mass ratio 1:8, corrosive acid potassium is added in 1% hydrochloric acid solution of mass fraction, stirs mixed rear and stands for 24 hours, filtering And filter residue is collected, it is 7.0 to be rinsed to cleaning solution pH with deionized water, then the dry 5h at 80 DEG C, grinds to obtain modified particles;To nothing Water-ethanol is passed through nitrogen, and it is 30mL/min that control nitrogen, which is passed through rate, and nitrogen 30min to be led to obtains modification liquid, then in parts by weight Meter weighs 50 parts of modification liquids, 15 parts of deionized waters, 30 parts of absolute ethyl alcohols, 15 parts of tetraethoxysilanes and is placed in three-necked flask respectively In, at 50 DEG C after insulation reaction 5h, obtain mixed liquor and by volume 1:8, γ-aminopropyl tetraethoxysilane is added dropwise to mixed It closes in liquid, control drop rate is 3mL/min, after being added dropwise to complete, then reacts 12h at 85 DEG C, collects to obtain reaction solution juxtaposition In dialysis membrane, is dialysed using absolute ethyl alcohol and collect dialysis modification liquid;In mass ratio 1:5, by Sodium Allyl Sulfonate and 12 Alkyl trimethyl ammonium chloride is stirred and 1% sodium hydroxide solution of mass fraction is used to adjust pH to 9.0, obtains matrix liquid and by weight Number meter is measured, 50 parts of matrix liquid, 15 parts of dialysis modification liquids, 20 parts of modified particles and 5 parts of polyvinyl alcohol is weighed respectively and is placed in beaker In, it is stirred and adjusts pH to 9.0 with 1% sodium hydroxide solution of mass fraction, obtain modified mixed liquor, modified mixed liquor is set In three-necked flask, at 85 DEG C, in mass ratio 1:15,1% ammonium persulfate solution of mass fraction is added dropwise to modified mixed liquor In, control ammonium persulfate drop rate is 3mL/min, and after being added dropwise to complete, then the insulation reaction 5h at 85 DEG C, standing are cooled to Room temperature, then the ultrasonic disperse 15min at 300W, you can be prepared into the low metal responsive type coal water slurry dispersing agent.
1,2,3 pairs of water-coal-slurry of example prepared by the present invention are added, control additive amount is 0.75%, and to water coal Slurry is tested for the property, and specific test result is as follows shown in table table 1:
1 performance test table of table
As seen from the above table, the present invention, which prepares coal water slurry dispersing agent, has excellent dispersion performance and resistance to metal ion disturbance performance.

Claims (3)

1. a kind of preparation method of low metal responsive type coal water slurry dispersing agent, it is characterised in that specifically preparation process is:
(1)In mass ratio 1:8, corrosive acid potassium is added in hydrochloric acid solution, stirs mixed rear and stands, filter and collect filter residue, Washing, drying, grind to obtain modified particles;Nitrogen is passed through to absolute ethyl alcohol, leads to nitrogen treatment, obtains modification liquid;
(2)Count in parts by weight, respectively weigh 45~50 parts of modification liquids, 10~15 parts of deionized waters, 25~30 parts of absolute ethyl alcohols, 10~15 parts of tetraethoxysilanes are placed in three-necked flask, and insulation reaction obtains mixed liquor and by volume 1:8, by γ-aminopropyl Tetraethoxysilane is added dropwise in mixed liquor, and after being added dropwise to complete, heating in water bath for reaction collects to obtain reaction solution;
(3)It places reaction liquid into dialysis membrane, dialysed using absolute ethyl alcohol and collects dialysis modification liquid, in mass ratio 1:5, by alkene Propyl sulfonic acid sodium is stirred and adjusts pH to 9.0 with dodecyl trimethyl ammonium chloride, obtains matrix liquid;
(4)It counts in parts by weight, weighs 45~50 parts of matrix liquid, 10~15 parts of dialysis modification liquids, 15~20 parts of modifications respectively Grain and 3~5 parts of polyvinyl alcohol are placed in beaker, are stirred and are adjusted pH to 9.0, obtain modified mixed liquor;
(5)Modified mixed liquor is placed in three-necked flask, at 75~85 DEG C, in mass ratio 1:15, ammonium persulfate solution is dripped It adds in modified mixed liquor, after being added dropwise to complete, insulation reaction, standing is cooled to room temperature, ultrasonic disperse, you can be prepared into described Low metal responsive type coal water slurry dispersing agent.
2. a kind of preparation method of low metal responsive type coal water slurry dispersing agent according to claim 1, it is characterised in that:Step Suddenly(1)It is 25~30mL/min that the nitrogen, which is passed through rate,.
3. a kind of preparation method of low metal responsive type coal water slurry dispersing agent according to claim 1, it is characterised in that:Step Suddenly(2)The γ-aminopropyl tetraethoxysilane drop rate is 2~3mL/min.
CN201810372355.1A 2018-04-24 2018-04-24 A kind of preparation method of low metal responsive type coal water slurry dispersing agent Withdrawn CN108531231A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810372355.1A CN108531231A (en) 2018-04-24 2018-04-24 A kind of preparation method of low metal responsive type coal water slurry dispersing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810372355.1A CN108531231A (en) 2018-04-24 2018-04-24 A kind of preparation method of low metal responsive type coal water slurry dispersing agent

Publications (1)

Publication Number Publication Date
CN108531231A true CN108531231A (en) 2018-09-14

Family

ID=63478287

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810372355.1A Withdrawn CN108531231A (en) 2018-04-24 2018-04-24 A kind of preparation method of low metal responsive type coal water slurry dispersing agent

Country Status (1)

Country Link
CN (1) CN108531231A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103951836A (en) * 2014-04-18 2014-07-30 陕西科技大学 Method for preparing sulfonation condensation polymerization modified humic acid water-coal-slurry dispersing agent
CN103951835A (en) * 2014-04-18 2014-07-30 陕西科技大学 Preparation method of polyaldehyde crosslinked sulfomethylated humate coal water slurry dispersant
CN104152195A (en) * 2014-08-01 2014-11-19 陕西科技大学 Amphoteric humate coal water slurry dispersant as well as preparation and application thereof
CN104193920A (en) * 2014-08-01 2014-12-10 陕西科技大学 Amphiprotic humic acid grafted copolymer coal water slurry dispersing agent as well as preparation and application thereof
CN105542886A (en) * 2014-11-03 2016-05-04 太原市天鼎恒砼外加剂科技发展有限公司 Coal water slurry dispersant and preparation method thereof
CN105567354A (en) * 2014-10-13 2016-05-11 太原市天鼎恒硂外加剂科技发展有限公司 Dispersant for coal water slurry and preparation method thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103951836A (en) * 2014-04-18 2014-07-30 陕西科技大学 Method for preparing sulfonation condensation polymerization modified humic acid water-coal-slurry dispersing agent
CN103951835A (en) * 2014-04-18 2014-07-30 陕西科技大学 Preparation method of polyaldehyde crosslinked sulfomethylated humate coal water slurry dispersant
CN104152195A (en) * 2014-08-01 2014-11-19 陕西科技大学 Amphoteric humate coal water slurry dispersant as well as preparation and application thereof
CN104193920A (en) * 2014-08-01 2014-12-10 陕西科技大学 Amphiprotic humic acid grafted copolymer coal water slurry dispersing agent as well as preparation and application thereof
CN105567354A (en) * 2014-10-13 2016-05-11 太原市天鼎恒硂外加剂科技发展有限公司 Dispersant for coal water slurry and preparation method thereof
CN105542886A (en) * 2014-11-03 2016-05-04 太原市天鼎恒砼外加剂科技发展有限公司 Coal water slurry dispersant and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
卢家烂: "《金属成矿中的有机地球化学研究》", 31 December 2004, 广东科技出版社 *

Similar Documents

Publication Publication Date Title
CN108557828A (en) A kind of preparation method of the special flatting silica of elastomeric paint
CN102796460B (en) Silicon dioxide-based CMP (Chemical Mechanical Polishing) solution and preparation method thereof
CN103450487B (en) The Nano-meter SiO_2 that a kind of hydrophilic and hydrophobic is adjustable 2powder
CN104946202A (en) Iron-doped silica sol composite abrasive grain, and polishing solution composition and preparation method thereof
CN103030151A (en) Neutral large-particle-size high-concentration and high-purity silica solution, and preparation and use of the same
CN111392739B (en) Preparation method and application of high-dispersity thickening type silicon dioxide
CN108083283B (en) Aluminum modified acidic silica sol and preparation method thereof
CN103896290A (en) Stable modified silica solution and preparation method thereof
CN106433221B (en) A kind of superfine heavy calcium carbonate and preparation method thereof that single layer is silicate modified
CN104327654A (en) Sun-reflection heat-insulation paint and manufacturing method thereof
CN103497340A (en) Preparation method of water-soluble polystyrene-silicon dioxide core-shell type composite particle
CN108531231A (en) A kind of preparation method of low metal responsive type coal water slurry dispersing agent
CN109872831A (en) Compound silver paste of modified graphene and preparation method thereof
CN103936019A (en) Method for preparing uniform magnetic nano silicon dioxide grain
CN105647478A (en) Nickel element doped silicon dioxide composite abrasive particle, polishing solution composition and preparation method of polishing solution composition
CN103589344B (en) Method for preparing alumina polishing solution
CN103482681A (en) Method for preparing monodisperse spherical nano ZnO
CN104211072A (en) Nano silicon dioxide production process technology
CN108751179A (en) A kind of preparation method of transparent graphene conductive film
CN106467670B (en) A kind of preparation method of silver nanoparticle mixed fillers modified silicon rubber conducing composite material
Xu et al. Surface modification of nano-silica with silane coupling agent
CN105176492A (en) Lanthanum-doped silicon dioxide sol composite abrasive particles, polishing solution composition and preparation methods of lanthanum-doped silicon dioxide sol composite abrasive particles and polishing solution composition
CN101265432A (en) Method for preparing nano microcrystal cellulose electric rheologic liquid
CN115417415A (en) Silicon dioxide for high-transparency silicone rubber and preparation method and application thereof
CN102010658B (en) Preparation method of chemical and mechanical polishing liquid of tungsten-molybdenum alloy material

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20180914

WW01 Invention patent application withdrawn after publication