[go: up one dir, main page]

WO2024125545A1 - Quaternary ammonium salt polyether ester monomer, epeg type polycarboxylate water reducing agent, and preparation method therefor - Google Patents

Quaternary ammonium salt polyether ester monomer, epeg type polycarboxylate water reducing agent, and preparation method therefor Download PDF

Info

Publication number
WO2024125545A1
WO2024125545A1 PCT/CN2023/138385 CN2023138385W WO2024125545A1 WO 2024125545 A1 WO2024125545 A1 WO 2024125545A1 CN 2023138385 W CN2023138385 W CN 2023138385W WO 2024125545 A1 WO2024125545 A1 WO 2024125545A1
Authority
WO
WIPO (PCT)
Prior art keywords
quaternary ammonium
ammonium salt
diethylene glycol
epeg
monomer
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.)
Ceased
Application number
PCT/CN2023/138385
Other languages
French (fr)
Chinese (zh)
Inventor
王昭鹏
方云辉
钟丽娜
柯余良
林泽宇
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.)
Kezhijie New Material Group Co Ltd
Original Assignee
Kezhijie New Material Group 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 Kezhijie New Material Group Co Ltd filed Critical Kezhijie New Material Group Co Ltd
Publication of WO2024125545A1 publication Critical patent/WO2024125545A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F283/00Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C08F283/06Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
    • C08F283/065Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals on to unsaturated polyethers, polyoxymethylenes or polyacetals
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24Macromolecular compounds
    • C04B24/243Phosphorus-containing polymers
    • C04B24/246Phosphorus-containing polymers containing polyether side chains
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2103/00Function or property of ingredients for mortars, concrete or artificial stone
    • C04B2103/30Water reducers, plasticisers, air-entrainers, flow improvers
    • C04B2103/302Water reducers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Definitions

  • the invention relates to the technical field of concrete admixtures, and in particular to a quaternary ammonium salt polyether ester monomer, an EPEG type polycarboxylate water reducer and a preparation method thereof.
  • the viscosity reduction performance of high-grade concrete is achieved mainly through three ways: increasing the amount of water reducer, selecting high-quality ultrafine powder, and optimizing particle grading.
  • increasing the amount of water reducer will not only increase production costs, but may also cause excessive slow setting of concrete, resulting in problems such as water seepage and bottoming, increasing the difficulty of construction and easily causing engineering accidents;
  • the selection of high-quality ultrafine powder is limited by the regionality and quality stability of the adhesive, and optimizing the particle grading can improve the viscosity and fluidity of the initial high-strength concrete to a certain extent, but it cannot fundamentally solve the problem.
  • polycarboxylate water reducer As the third generation of high-performance water reducers, polycarboxylate water reducer (PCE) has the characteristics of low dosage, high water reduction rate, and green environmental protection. It can significantly improve the working performance, mechanical properties and durability of concrete. It has gradually become the fifth indispensable component in the mix design of commercial concrete in addition to water, sand, stone, admixtures and cement.
  • the differences in the synthetic raw materials and preparation methods of PCE determine its molecular structure, which in turn affects the working, mechanical and durability properties of concrete in engineering applications.
  • ethylene glycol monovinyl polyethylene glycol ether (EPEG) is a new type of 6C polyether macromonomer, which has the advantages of high reactivity, good adaptability, strong structural designability, and easy regulation.
  • an EPEG type polycarboxylate water-reducing agent that can effectively reduce the viscosity of concrete and improve the workability of concrete is developed from the perspective of the designable structure of the polycarboxylate water-reducing agent, which is of great significance to the development of the construction industry.
  • the present invention provides an EPEG type polycarboxylate water reducer, and its technical solution is as follows:
  • the copolymer is polymerized by comonomers, wherein the comonomers include ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomers, unsaturated carboxylic acid monomers, unsaturated sulfonates, silane monomers, allyl dimethyl phosphate chloride and quaternary ammonium salt polyether ester monomers;
  • the comonomers include ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomers, unsaturated carboxylic acid monomers, unsaturated sulfonates, silane monomers, allyl dimethyl phosphate chloride and quaternary ammonium salt polyether ester monomers;
  • the weight ratio of the ethylene glycol monovinyl polyethylene glycol ether, the unsaturated amide monomer, the unsaturated carboxylic acid monomer, the unsaturated sulfonate, the silane monomer, the dimethyl chloride allyl phosphate and the quaternary ammonium salt polyether ester monomer is (200-300): (4-8): (20-30): (4-8): (2-4): (4-6): (4-6).
  • it is prepared by copolymerizing ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomer, unsaturated carboxylic acid monomer, unsaturated sulfonate, silane monomer, allyl dimethyl phosphate chloride and quaternary ammonium salt polyether ester monomer at 10°C to 15°C.
  • the unsaturated amide monomer is one or more combinations of acrylamide, N-(2-dimethylaminoethyl)acrylamide, N,N-methylenebisacrylamide, cyclopropaneamide, and caprolactam;
  • the monomer is one or more combinations of acrylic acid, methacrylic acid, fumaric acid, maleic anhydride, and itaconic acid;
  • the unsaturated sulfonate is one or more combinations of sodium methyl propylene sulfonate, sodium styrene sulfonate, 2-acrylamide-2-methylpropane sulfonic acid, and sodium dodecylbenzene sulfonate;
  • the silane monomer is one or more combinations of vinyl trimethoxy silane, vinyl triethoxy silane, ⁇ -methacryloxypropyl trimethoxy silane, KH550, and KH570;
  • the quaternary ammonium salt polyether ester monomer is a blocked qua
  • the chloroallyl dimethyl phosphate is prepared by esterification of dimethyl allyl phosphate and thionyl chloride; the weight ratio of the dimethyl allyl phosphate to the thionyl chloride is 100:(100-150).
  • the preparation method of allyl dimethyl phosphate chloride is as follows: allyl dimethyl phosphate and solvent A are mixed, and a first catalyst and an inhibitor are added, the reaction system is heated to 40°C to 60°C, and thionyl chloride is added to the reaction system, and an esterification reaction is carried out at 40°C to 60°C for 2 to 4 hours and the temperature is kept for 3 to 5 hours to obtain the allyl dimethyl phosphate chloride; wherein the preparation of the allyl dimethyl phosphate chloride is carried out under a nitrogen atmosphere or an inert atmosphere; the weight ratio of the allyl dimethyl phosphate, solvent A, thionyl chloride, the first catalyst and the inhibitor is 100:(350-400):(100-150):(5-10):(0.5-1.0).
  • the solvent A is one or more combinations of dichloromethane, chloroform, acetonitrile, and toluene;
  • the first catalyst is one or more combinations of N'N dimethylformamide, pyridine, 4-dimethylaminopyridine, concentrated sulfuric acid, and ethyl sulfonic acid;
  • the inhibitor is one or more combinations of hydroquinone, p-hydroxyanisole, phenothiazine, cuprous chloride, and ferric chloride.
  • the preparation method of the quaternary ammonium salt polyether ester monomer is as follows: diethylene glycol monoallyl ether, amino acid, and a second catalyst are added to a reaction kettle and mixed evenly, reacted at 60° C. to 120° C. for 2 to 8 hours, and then cooled to room temperature, and then chloroform is added to the reaction kettle, mixed evenly, and allowed to stand for 12 to 24 hours to obtain diethylene glycol monoallyl ether carboxylate;
  • diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A to dissolve, and then pyridine is added to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate;
  • the obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under nitrogen atmosphere or inert atmosphere, and the reaction system is heated to 40°C to 60°C for 5h to 12h to obtain acyl Chlorinated diethylene glycol monoallyl ether carboxylate;
  • acyl chloride diethylene glycol monoallyl ether carboxylate is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the reaction is carried out at 65°C to 90°C for 5 to 24 hours to obtain a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, that is, a quaternary ammonium salt polyether ester monomer is obtained.
  • the amino acid is one or more combinations of glutamic acid and aspartic acid;
  • the solvent A is one or more combinations of dichloromethane, chloroform, acetonitrile, and toluene;
  • the second catalyst is one or more combinations of thionyl chloride, copper sulfate, and tetrabutyl titanate;
  • the unsaturated acid anhydride is one or more combinations of maleic anhydride and succinic anhydride;
  • the quaternary ammonium salt compound is one or more combinations of ammonium chloride, methacryloyloxyethyltrimethylammonium chloride, dimethylalkylammonium chloride, benzyltrimethylammonium chloride, and chlormequat.
  • the present invention also provides a method for preparing the EPEG type polycarboxylate water reducer as described above, which comprises the following steps:
  • Unsaturated carboxylic acid monomer, quaternary ammonium salt polyether ester monomer, unsaturated sulfonate, chain transfer agent and reducing agent are added to the base liquid, and copolymerization reaction is carried out at 10° C. to 15° C. to prepare the EPEG type polycarboxylate water reducer.
  • the present invention also provides a quaternary ammonium salt polyether ester monomer, and the preparation method thereof is as follows:
  • diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A to dissolve, and then pyridine is added to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate;
  • the obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under a nitrogen atmosphere or an inert atmosphere, and the reaction system is heated to 40°C to 60°C for 5h to 12h to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;
  • the obtained diethylene glycol monoallyl ether carboxylate acylation is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the mixture is reacted at 65°C to 90°C for 5 to 24 hours to obtain a quaternary ammonium salt polyether ester monomer.
  • the EPEG type polycarboxylate water reducer provided by the present invention has the following beneficial effects:
  • the EPEG type polycarboxylate water-reducing agent provided by the present invention can effectively reduce the viscosity of concrete, improve the workability and flow rate of concrete, and improve the mechanical properties of concrete; it has the advantages of low dosage, high water reduction rate, good workability, and can significantly reduce the viscosity of slurry.
  • the present invention provides a preferred embodiment of the preparation method of the EPEG type polycarboxylate water reducer, which specifically comprises the following steps:
  • Step a) dissolving ethylene glycol monovinyl polyethylene glycol ether (EPEG) in water, placing in a reactor, and stirring thoroughly. Mix well;
  • EPEG ethylene glycol monovinyl polyethylene glycol ether
  • the raw materials in the copolymerization reaction system include 200-300 parts of ethylene glycol monovinyl polyethylene glycol ether, 4-8 parts of unsaturated amide monomers, 20-30 parts of unsaturated carboxylic acid monomers, 4-8 parts of unsaturated sulfonates, 2-4 parts of silane monomers, 4-6 parts of dimethyl chloroallyl phosphate, 4-6 parts of quaternary ammonium salt polyether ester monomers, 2.5-4.5 parts of oxidants, 0.2-0.4 parts of reducing agents, 1-1.5 parts of chain transfer agents, 1-2 parts of sulfates, and 350-400 parts of water.
  • the overall acid-ether ratio is 1.0-2.0.
  • the present invention also provides a preferred embodiment of its preparation method as follows:
  • the chlorinated allyl dimethyl phosphate is prepared by esterification reaction of allyl dimethyl phosphate and thionyl chloride; the specific process is:
  • Allyl dimethyl phosphate and solvent A are stirred at room temperature for 0.5 to 2 hours to mix; and a first catalyst and a polymerization inhibitor are added, the reaction system is heated to 40°C to 60°C, thionyl chloride is added dropwise at this temperature for esterification reaction for 2 to 4 hours and kept warm for 3 to 5 hours, and after the reaction is completed, the allyl dimethyl phosphate is filtered and subjected to rotary evaporation to obtain the allyl dimethyl phosphate; wherein the preparation of the allyl dimethyl phosphate is carried out under a nitrogen atmosphere or an inert atmosphere throughout the reaction;
  • the weight ratio of allyl dimethyl phosphate, solvent A, thionyl chloride, the first catalyst and the polymerization inhibitor is 100: (350-400): (100-150): (5-10): (0.5-1.0).
  • the solvent A may be preferably one or more of dichloromethane, chloroform, acetonitrile, and toluene;
  • the first catalyst may be preferably N'N-dimethylformamide, pyridine, 4-dimethylaminopyridine, concentrated sulfuric acid, ethylsulfonic acid, One or more combinations of;
  • the inhibitor may preferably be one or more combinations of hydroquinone, p-hydroxyanisole, phenothiazine, cuprous chloride, and ferric chloride.
  • the present invention also provides a preferred embodiment of the preparation method of the quaternary ammonium salt polyether ester monomer as follows:
  • diethylene glycol monoallyl ether, amino acid and a second catalyst are added to a reaction kettle and stirred to mix evenly, reacted at 60°C to 120°C for 2 to 8 hours and then cooled to room temperature, and then chloroform is added to the reaction kettle and mixed evenly and allowed to stand for 12 to 24 hours, filtered, and the filtrate is evaporated under reduced pressure at 50°C to 65°C to remove chloroform, thereby separating and obtaining diethylene glycol monoallyl ether carboxylate; wherein the weight ratio of diethylene glycol monoallyl ether to chloroform is 1:(1 to 3);
  • the obtained diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A, stirred and dissolved, and then pyridine is added dropwise to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate; wherein the reaction temperature is controlled at (40° C. to 60° C.);
  • the obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under a nitrogen atmosphere or an inert atmosphere, the reaction system is heated to 40°C to 60°C for 5h to 12h, the thionyl chloride is removed by concentration under reduced pressure, and the product is washed with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;
  • acyl chloride diethylene glycol monoallyl ether carboxylate is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the reaction is carried out at 65°C to 90°C for 5 to 24 hours.
  • a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate is obtained, i.e., a quaternary ammonium salt polyether ester monomer is obtained.
  • the weight ratio of diethylene glycol monoallyl ether, amino acid, unsaturated acid anhydride, thionyl chloride and quaternary ammonium salt compound is (100-200): (65-130): (60-120): (200-400): (2-6);
  • the amino acid can be preferably one or more combinations of glutamic acid and aspartic acid;
  • the solvent A can be preferably one or more combinations of dichloromethane, chloroform, acetonitrile and toluene;
  • the second catalyst can be preferably one or more combinations of thionyl chloride, copper sulfate and tetrabutyl titanate;
  • the unsaturated acid anhydride can be preferably one or more combinations of maleic anhydride and succinic anhydride;
  • the quaternary ammonium salt compound can be preferably one or more combinations of ammonium chloride, methacryloyloxyethyl trimethylammonium chloride, dimethyl alkyl ammonium chloride, benzyl trimethyl ammonium chloride and chlormequat.
  • the amino acid Aspartic acid is selected; the solvent A is chloroform; the second catalyst is copper sulfate; the unsaturated acid anhydride is succinic anhydride; and the quaternary ammonium salt compound is dimethyl alkyl ammonium chloride.
  • the unsaturated amide monomer may preferably be one or more combinations of acrylamide, N-(2-dimethylaminoethyl)acrylamide, N,N-methylenebisacrylamide, cyclopropaneamide, and caprolactam;
  • the unsaturated carboxylic acid monomer may preferably be one or more combinations of acrylic acid, methacrylic acid, fumaric acid, maleic anhydride, and itaconic acid;
  • the unsaturated sulfonate may preferably be one or more combinations of sodium methyl propylene sulfonate, sodium styrene sulfonate, 2-acrylamide-2-methylpropane sulfonic acid, and sodium dodecylbenzene sulfonate;
  • the silane monomer may preferably be one or more combinations of vinyl trimethoxy silane, vinyl triethoxy silane, ⁇ -methacryloxypropyl trimethoxy silane, KH550, and KH570.
  • the reducing agent is preferably one or more combinations of sodium sulfite, bleaching powder, sodium bisulfite, and sodium hypophosphite, wherein sodium hypophosphite can also be used as a chain transfer agent;
  • the oxidizing agent may be preferably one or more combinations of hydrogen peroxide, sodium peroxide, potassium peroxide, magnesium peroxide, sodium persulfate, ammonium persulfate, sodium dichromate, potassium dichromate, and potassium permanganate;
  • the chain transfer agent may be preferably one or more combinations of thioglycolic acid, sodium hypophosphite, trisodium phosphate, mercaptopropionic acid, mercaptoethanol, and thioglycolic acid.
  • the sulfate is preferably ferrous sulfate.
  • the silane monomer is KH550;
  • the unsaturated carboxylic acid monomer is acrylic acid; and the oxidizing agent is hydrogen peroxide.
  • a catalyst copper sulfate
  • Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.
  • allyl dimethyl phosphate 100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.
  • a catalyst copper sulfate
  • Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.
  • liquid A by mixing 20g of acrylic acid, 4g of quaternary ammonium salt polyether ester monomer, and 30g of water; prepare liquid B by mixing 4g of AMPS, 0.8g of mercaptopropionic acid monomer, and 50g of water; prepare liquid C by mixing 0.25g of bleaching powder and 50g of water.
  • liquid B by mixing 4g of AMPS, 0.8g of mercaptopropionic acid monomer, and 50g of water
  • liquid C by mixing 0.25g of bleaching powder and 50g of water.
  • liquids A and B added for 50min
  • liquid C added for 60min; keep warm for 1h after the addition is completed, and the temperature does not exceed 25°C throughout the process.
  • liquid is added to adjust the pH value of the solution to be controlled at 5.0-6.5 to obtain an EPEG type polycarboxylate water reducer.
  • allyl dimethyl phosphate 100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.
  • a catalyst copper sulfate
  • Step b) 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride were added to 300ml of chloroform and stirred to dissolve, and then the temperature was raised to 60°C, and 15g of pyridine was added dropwise at this temperature for 3h. After the reaction, chloroform and saturated sodium bicarbonate solution were added for extraction, and the organic phase was dried and washed with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, which was then dissolved in N,N-dimethylformamide, and 200mL of chlorinated amine was added dropwise in a nitrogen atmosphere. sulfone, heating to 60°C for 8h, concentrating under reduced pressure to remove thionyl chloride, washing the product with ether to obtain diethylene glycol monoallyl ether carboxylate;
  • Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.
  • allyl dimethyl phosphate 100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.
  • a catalyst copper sulfate
  • Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.
  • allyl dimethyl phosphate 100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.
  • a catalyst copper sulfate
  • Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.
  • liquid A with 20g of acrylic acid, 4g of quaternary ammonium salt polyether ester monomer, and 30g of water; prepare liquid B with 4g of sodium methyl propylene sulfonate, 1.2g of mercaptopropionic acid monomer, and 50g of water; prepare liquid C with 0.25g of bleaching powder and 50g of water.
  • liquid A and liquid B are added for 50min, and liquid C is added for 60min; after the addition is completed, keep warm for 1h, and the temperature does not exceed 25°C throughout the process. After the heat preservation is completed, liquid is added to adjust the pH value of the solution to be controlled at 5.0-6.5 to obtain an EPEG type polycarboxylate water reducer.
  • a catalyst copper sulfate
  • Step c) 100 g of diethylene glycol monoallyl ether carboxylate was added to a four-necked flask, and after repeated dissolution with 100 ml of DMF solution, the temperature was raised to 80° C., 5.8 g of ethanolamine was added, and the mixture was condensed and refluxed for 12 h, and then 2.2 g of After dimethyl alkyl ammonium chloride and 20 ml of DMF solution were added dropwise for 1 hour, the mixture was condensed and refluxed for 12 hours, all under a nitrogen atmosphere. After the reaction was completed, the reaction product was filtered and rotary evaporated to prepare a blocked quaternary ammonium salt of diethylene glycol monoallyl ether carboxylate.
  • allyl dimethyl phosphate 100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.
  • Runfeng cement (PO 42.5), machine-made sand and crushed stone were used as raw materials.
  • the concrete mix ratio was: cement 360kg/m 3 , fly ash (grade II) 80kg/m 3 , mineral powder 60kg/m 3 , sand 750kg/m 3 , gravel 980kg/m 3 , and the expansion was controlled at 650 ⁇ 20mm.
  • the polycarboxylate water-reducing agent samples of the embodiment and the comparative example were respectively tested for initial slump and expansion of the concrete, slump and expansion over time, emptying time of the inverted slump bucket, and emptying time of the inverted slump bucket over time according to GB8076-2008 "Concrete Admixtures", GB 8077-2012 “Test Method for Homogeneity of Concrete Admixtures” and GJ281-2012 “Technical Specification for Application of High-Strength Concrete”.
  • the test results are shown in Table 1:
  • Comparative Example 2 The only difference between Comparative Example 2 and Example 4 is that no dimethyl chloroallyl phosphate is added in the copolymerization reaction. Compared with Example 4, the emptying time of Comparative Example 2 is significantly increased, indicating that the viscosity of the concrete in Comparative Example 2 is large. This is because the phosphate introduced in the scheme of the present invention has a strong adsorption capacity for cement, which is beneficial to its wetting and adsorption of cement, improves the dispersibility and fluidity of concrete, and reduces the viscosity of concrete.
  • Comparative Example 3 The only difference between Comparative Example 3 and Example 4 is that no quaternary ammonium salt polyether ester monomer is added in the copolymerization reaction. Compared with Example 4, the emptying time of Comparative Example 3 is significantly increased, indicating that the concrete viscosity of Comparative Example 3 is large. This is because the quaternary ammonium salt group introduced in the scheme of the present invention can be electrostatically adsorbed on the surface of cement particles, thereby showing good dispersibility and fluidity, and effectively reducing the viscosity of the concrete.
  • Comparative Example 4 The only difference between Comparative Example 4 and Example 4 is that no dimethyl chlorinated allyl phosphate and quaternary ammonium salt polyether ester monomer are added in the copolymerization reaction. Compared with Example 4, the emptying time of Comparative Example 4 is significantly increased, indicating that the concrete of Comparative Example 4 The high viscosity indicates that the phosphate and quaternary ammonium salt groups introduced in the solution of the present invention can be effectively adsorbed on the surface of cement particles through electrostatic adsorption and steric hindrance, indicating that it has good fluidity and dispersibility.
  • the EPEG type polycarboxylate water-reducing agent provided in Examples 1-5 of the present invention has a short emptying time, which can effectively reduce the viscosity of concrete, and the reduced viscosity of concrete can improve the flow rate of concrete, so its construction performance becomes better and the workability of concrete is improved; under the condition of achieving the same expansion degree, the dosage and emptying time in the embodiment are lower than those in the comparative example; at the same time, the mechanical properties of the concrete in Examples 1-5 of the present invention remain good; in summary, the EPEG type polycarboxylate water-reducing agent prepared in the embodiment of the present invention has good viscosity reduction performance, can improve the workability and flow rate of concrete, and at the same time, it has a significant improvement on the mechanical properties of concrete without other adverse effects; the EPEG type polycarboxylate water-reducing agent has the advantages of wide applicability, simple and fast preparation process and high efficiency.
  • the EPEG type polycarboxylate water reducer and its preparation method provided by the present invention at least include the following design concepts, action mechanisms and beneficial effects:
  • the present invention is based on the designable structure of the polycarboxylate water-reducing agent, and the EPEG type polycarboxylate water-reducing agent is developed by molecular design.
  • the EPEG type polycarboxylate water-reducing agent is prepared by copolymerizing ethylene glycol monovinyl polyethylene glycol ether (EPEG), unsaturated amide monomers, unsaturated carboxylic acid monomers, unsaturated sulfonates, silane monomers, dimethyl chloroallyl phosphate and quaternary ammonium salt polyether ester monomers, and phosphate, carboxylate, amide, sulfonic acid, quaternary ammonium salt and silane groups are introduced into the polymer molecular structure.
  • EPEG ethylene glycol monovinyl polyethylene glycol ether
  • phosphate has a strong adsorption capacity for cement, and works synergistically with carboxylate, which is beneficial to its wetting and adsorption of cement, and improves the dispersibility and fluidity of concrete;
  • amide group protects carboxyl group to a certain extent, reduces the initial adsorption rate of carboxyl group in water reducer to cement particles, and gradually hydrolyzes in alkaline environment, and then releases carboxyl group, which will continue to slowly adsorb cement particles, thus showing good dispersibility and fluidity.
  • Silane group can introduce double-bonded alkoxysilane into the main chain of PCEs through free radical polymerization, and can chemically bond with cementitious materials after hydrolysis, and its binding ability is stronger than electrostatic adsorption, so the solid-liquid interface energy between cementitious material particles and liquid phase is low, the bound water on the surface of cementitious material particles is less, the water film thickness is small, and there is more free water in the system, thus showing good dispersibility and fluidity.
  • Quaternary ammonium salt group can be electrostatically adsorbed on the surface of cement particles, thereby showing good dispersibility.
  • the EPEG type polycarboxylate water reducer has the advantages of low dosage, good workability and the ability to significantly reduce the slurry viscosity.
  • the EPEG type polycarboxylate water reducer provided by the present invention has the advantages of low dosage, high water reduction rate, good workability, and can significantly reduce the viscosity of the slurry and has a wide adaptability to the mud content of sand and gravel.
  • the EPEG type polycarboxylate water reducer provided by the present invention has common and easily available raw materials required for its preparation process, low cost, and the preparation process is simple, fast, green and environmentally friendly.
  • the present invention develops the above-mentioned EPEG type polycarboxylate water-reducing agent from the perspective of the designable structure of the polycarboxylate water-reducing agent, and the EPEG type polycarboxylate water-reducing agent can effectively reduce the viscosity of concrete and improve the workability of concrete; it has the advantages of high water reduction, good concrete performance, good adaptability, simple process, etc. And its preparation method process has the advantages of cheap and easy availability of the required raw materials, environmental friendliness, easy control of reaction conditions, simple production process, low production cost, short synthesis time, high efficiency, low energy consumption, etc.
  • EPEG Ethylene glycol monovinyl polyethylene glycol ether
  • AMPS 2-acrylamide-2-methylpropane sulfonic acid

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Polyethers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

The present invention relates to the technical field of concrete admixtures, and in particular relates to a quaternary ammonium salt polyether ester monomer, an EPEG type polycarboxylate water reducing agent, and a preparation method therefor. The EPEG type polycarboxylate water reducing agent is formed by copolymerizing ethylene glycol monovinyl polyethylene glycol ether, an unsaturated amide monomer, an unsaturated carboxylic acid monomer, an unsaturated sulfonate, a silane monomer, dimethyl allyl phosphate chloride and a quaternary ammonium salt polyether ester monomer. The EPEG type polycarboxylate water reducing agent can effectively reduce the viscosity of concrete and improve the workability and flow rate of concrete, and has a significant improvement effect on the mechanical properties of concrete; and same has the advantages of a low amount, a high water-reducing rate, good workability, being capable of significantly reducing the viscosity of a slurry, wide applicability, etc.

Description

一种季铵盐聚醚酯单体、EPEG型聚羧酸减水剂及其制备方法A quaternary ammonium salt polyether ester monomer, EPEG type polycarboxylate water reducer and preparation method thereof

相关申请的交叉引用CROSS-REFERENCE TO RELATED APPLICATIONS

本申请要求于2022年12月16日提交中国专利局的申请号为202211621645.8、名称为《一种季铵盐聚醚酯单体、EPEG型聚羧酸减水剂及其制备方法》的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims the priority of Chinese patent application No. 202211621645.8, filed with the Chinese Patent Office on December 16, 2022, and entitled "A quaternary ammonium salt polyether ester monomer, EPEG type polycarboxylic acid water reducer and preparation method thereof", the entire contents of which are incorporated by reference in this application.

技术领域Technical Field

本发明涉及混凝土外加剂技术领域,特别涉及一种季铵盐聚醚酯单体、EPEG型聚羧酸减水剂及其制备方法。The invention relates to the technical field of concrete admixtures, and in particular to a quaternary ammonium salt polyether ester monomer, an EPEG type polycarboxylate water reducer and a preparation method thereof.

背景技术Background technique

近年来,随着大型建筑的崛起,一些地标建筑、超高层建筑、桥梁、隧道等快速发展,对混凝土结构强度和耐久性的要求越来越高;整体强度高、自重轻的高强度混凝土得以广泛应用。In recent years, with the rise of large-scale buildings, some landmark buildings, super-high-rise buildings, bridges, tunnels, etc. have developed rapidly, and the requirements for the strength and durability of concrete structures have become increasingly higher; high-strength concrete with high overall strength and light weight has been widely used.

由于高标号混凝土采用低水胶比以及大量胶凝材料,在实际应用中存在新拌混凝土粘度大、流速慢等问题,会对混凝土的运输、泵送、施工带来一系列制约因素。因此,本领域技术人员从材料构成、配合比设计这两个混凝土技术研究的核心问题出发:通过优化材料构成以及调整配合比设计以改善高强度混凝土拌合粘度高、流速慢等问题。Since high-grade concrete uses a low water-cement ratio and a large amount of cementitious materials, there are problems such as high viscosity and slow flow rate of freshly mixed concrete in actual applications, which will bring a series of constraints to the transportation, pumping and construction of concrete. Therefore, technical personnel in this field start from the two core issues of concrete technology research, material composition and mix design: by optimizing material composition and adjusting mix design to improve the problems of high viscosity and slow flow rate of high-strength concrete.

高标号混凝土在大多数工业应用中降粘性能的实现主要通过提高减水剂掺量、选用优质的超细粉料、优化颗粒级配三种途径。提高减水剂掺量既会增加生产成本,也可能导致混凝土过分缓凝,出现泌水、扒底等问题,增加施工难度的同时也容易引发工程事故;选用优质的超细粉料受限于胶材的地域性以及质量稳定性,优化颗粒级配能使初拌高强度混凝土的粘度和流动性在一定程度上得到改善,但并不能从根本上解决问题。 In most industrial applications, the viscosity reduction performance of high-grade concrete is achieved mainly through three ways: increasing the amount of water reducer, selecting high-quality ultrafine powder, and optimizing particle grading. Increasing the amount of water reducer will not only increase production costs, but may also cause excessive slow setting of concrete, resulting in problems such as water seepage and bottoming, increasing the difficulty of construction and easily causing engineering accidents; the selection of high-quality ultrafine powder is limited by the regionality and quality stability of the adhesive, and optimizing the particle grading can improve the viscosity and fluidity of the initial high-strength concrete to a certain extent, but it cannot fundamentally solve the problem.

聚羧酸减水剂(PCE)作为第三代高性能减水剂,具有掺量低、减水率高、绿色环保等特点,能够显著改善混凝土的工作性能、力学性能和耐久性能,已逐渐成为商品混凝土配合比设计中除水、砂、石、掺合料、水泥之外必不可少的第五组分。PCE的合成原料和制备方法的差异决定其分子结构,进而影响混凝土在工程应用中的工作、力学和耐久性能。其中乙二醇单乙烯基聚乙二醇醚(EPEG)作为新型的6C聚醚大单体,其具有反应活性高、适应性好、结构可设计性强,易于调控等优势。As the third generation of high-performance water reducers, polycarboxylate water reducer (PCE) has the characteristics of low dosage, high water reduction rate, and green environmental protection. It can significantly improve the working performance, mechanical properties and durability of concrete. It has gradually become the fifth indispensable component in the mix design of commercial concrete in addition to water, sand, stone, admixtures and cement. The differences in the synthetic raw materials and preparation methods of PCE determine its molecular structure, which in turn affects the working, mechanical and durability properties of concrete in engineering applications. Among them, ethylene glycol monovinyl polyethylene glycol ether (EPEG) is a new type of 6C polyether macromonomer, which has the advantages of high reactivity, good adaptability, strong structural designability, and easy regulation.

因此,为解决高标号混凝土粘度大、流速慢、泵送困难的问题,通过聚羧酸减水剂结构可设计的角度,研制一种能够有效降低混凝土粘度,提升混凝土和易性的EPEG型聚羧酸减水剂,对建筑行业的发展都具有重要的意义。Therefore, in order to solve the problems of high viscosity, slow flow rate and difficult pumping of high-grade concrete, an EPEG type polycarboxylate water-reducing agent that can effectively reduce the viscosity of concrete and improve the workability of concrete is developed from the perspective of the designable structure of the polycarboxylate water-reducing agent, which is of great significance to the development of the construction industry.

发明内容Summary of the invention

为解决上述背景技术中提到的高标号混凝土粘度大、泵送困难的问题,本发明提供一种EPEG型聚羧酸减水剂,其技术方案如下:In order to solve the problem of high viscosity and difficult pumping of high-grade concrete mentioned in the above background technology, the present invention provides an EPEG type polycarboxylate water reducer, and its technical solution is as follows:

由共聚单体聚合而成,所述共聚单体包括乙二醇单乙烯基聚乙二醇醚、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯以及季铵盐聚醚酯单体;The copolymer is polymerized by comonomers, wherein the comonomers include ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomers, unsaturated carboxylic acid monomers, unsaturated sulfonates, silane monomers, allyl dimethyl phosphate chloride and quaternary ammonium salt polyether ester monomers;

所述乙二醇单乙烯基聚乙二醇醚、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯以及季铵盐聚醚酯单体的重量比为(200~300):(4~8):(20~30):(4~8):(2~4):(4~6):(4~6)。The weight ratio of the ethylene glycol monovinyl polyethylene glycol ether, the unsaturated amide monomer, the unsaturated carboxylic acid monomer, the unsaturated sulfonate, the silane monomer, the dimethyl chloride allyl phosphate and the quaternary ammonium salt polyether ester monomer is (200-300): (4-8): (20-30): (4-8): (2-4): (4-6): (4-6).

在一实施例中,其由乙二醇单乙烯基聚乙二醇醚、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯以及季铵盐聚醚酯单体于10℃~15℃下进行共聚反应制得。In one embodiment, it is prepared by copolymerizing ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomer, unsaturated carboxylic acid monomer, unsaturated sulfonate, silane monomer, allyl dimethyl phosphate chloride and quaternary ammonium salt polyether ester monomer at 10°C to 15°C.

在一实施例中,所述不饱和酰胺单体为丙烯酰胺、N-(2-二甲氨基乙基)丙烯酰胺、N,N-亚甲基双丙烯酰胺、环丙酰胺、己内酰胺中的一种或多种组合;所述不饱和羧酸单 体为丙烯酸、甲基丙烯酸、富马酸、马来酸酐、衣康酸中的一种或多种组合;所述不饱和磺酸盐为甲基丙烯磺酸钠、苯乙烯磺酸钠、2-丙烯酰胺-2-甲基丙磺酸、十二烷基苯磺酸钠中的一种或多种组合;所述硅烷单体为乙烯基三甲氧基硅烷、乙烯基三乙氧硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、KH550、KH570中的一种或多种组合;所述季铵盐聚醚酯单体为封端季铵盐二乙二醇单烯丙基醚羧酸酯。In one embodiment, the unsaturated amide monomer is one or more combinations of acrylamide, N-(2-dimethylaminoethyl)acrylamide, N,N-methylenebisacrylamide, cyclopropaneamide, and caprolactam; The monomer is one or more combinations of acrylic acid, methacrylic acid, fumaric acid, maleic anhydride, and itaconic acid; the unsaturated sulfonate is one or more combinations of sodium methyl propylene sulfonate, sodium styrene sulfonate, 2-acrylamide-2-methylpropane sulfonic acid, and sodium dodecylbenzene sulfonate; the silane monomer is one or more combinations of vinyl trimethoxy silane, vinyl triethoxy silane, γ-methacryloxypropyl trimethoxy silane, KH550, and KH570; the quaternary ammonium salt polyether ester monomer is a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.

在一实施例中,所述氯化烯丙基磷酸二甲酯由烯丙基磷酸二甲酯与氯化亚砜进行酯化反应制得;所述烯丙基磷酸二甲酯与所述氯化亚砜的重量比为100:(100~150)。In one embodiment, the chloroallyl dimethyl phosphate is prepared by esterification of dimethyl allyl phosphate and thionyl chloride; the weight ratio of the dimethyl allyl phosphate to the thionyl chloride is 100:(100-150).

在一实施例中,所述氯化烯丙基磷酸二甲酯的制备方法为:将烯丙基磷酸二甲酯和溶剂A混合,并加入第一催化剂和阻聚剂,反应体系升温至40℃~60℃,并向反应体系内加入氯化亚砜,在40℃~60℃下酯化反应2~4h并保温3~5h,制得所述氯化烯丙基磷酸二甲酯;其中,所述氯化烯丙基磷酸二甲酯的制备全程在氮气气氛或惰性气氛下进行反应;所述烯丙基磷酸二甲酯、溶剂A、氯化亚砜、第一催化剂与阻聚剂的重量比为100:(350~400):(100~150):(5~10):(0.5~1.0)。In one embodiment, the preparation method of allyl dimethyl phosphate chloride is as follows: allyl dimethyl phosphate and solvent A are mixed, and a first catalyst and an inhibitor are added, the reaction system is heated to 40°C to 60°C, and thionyl chloride is added to the reaction system, and an esterification reaction is carried out at 40°C to 60°C for 2 to 4 hours and the temperature is kept for 3 to 5 hours to obtain the allyl dimethyl phosphate chloride; wherein the preparation of the allyl dimethyl phosphate chloride is carried out under a nitrogen atmosphere or an inert atmosphere; the weight ratio of the allyl dimethyl phosphate, solvent A, thionyl chloride, the first catalyst and the inhibitor is 100:(350-400):(100-150):(5-10):(0.5-1.0).

在一实施例中,所述溶剂A为二氯甲烷、三氯甲烷、乙腈、甲苯中的一种或多种组合;所述第一催化剂为N’N二甲基甲酰胺、吡啶、4-二甲氨基吡啶、浓硫酸、乙基磺酸中的一种或多种组合;所述阻聚剂为对苯二酚、对羟基苯甲醚、吩噻嗪、氯化亚铜、氯化铁中的一种或多种组合。In one embodiment, the solvent A is one or more combinations of dichloromethane, chloroform, acetonitrile, and toluene; the first catalyst is one or more combinations of N'N dimethylformamide, pyridine, 4-dimethylaminopyridine, concentrated sulfuric acid, and ethyl sulfonic acid; the inhibitor is one or more combinations of hydroquinone, p-hydroxyanisole, phenothiazine, cuprous chloride, and ferric chloride.

在一实施例中,所述季铵盐聚醚酯单体的制备方法为:将二乙二醇单烯丙基醚、氨基酸、第二催化剂加入到反应釜内混合均匀,于60℃~120℃下反应2~8h后冷至室温,再将三氯甲烷加入到反应釜内混匀并静置12~24h后,即得二乙二醇单烯丙基醚羧酸酯;In one embodiment, the preparation method of the quaternary ammonium salt polyether ester monomer is as follows: diethylene glycol monoallyl ether, amino acid, and a second catalyst are added to a reaction kettle and mixed evenly, reacted at 60° C. to 120° C. for 2 to 8 hours, and then cooled to room temperature, and then chloroform is added to the reaction kettle, mixed evenly, and allowed to stand for 12 to 24 hours to obtain diethylene glycol monoallyl ether carboxylate;

将所得的二乙二醇单烯丙基醚羧酸酯,加入不饱和酸酐和溶剂A内溶解,而后加入吡啶进行反应,得到端羧基二乙二醇单烯丙基醚羧酸酯;The obtained diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A to dissolve, and then pyridine is added to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate;

将所得的端羧基二乙二醇单烯丙基醚羧酸酯溶解到N’N-二甲基甲酰胺中,在氮气气氛或惰性气氛下加入氯化亚砜,将反应体系升温至40℃~60℃反应5h~12h,制得酰 氯化二乙二醇单烯丙基醚羧酸酯;The obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under nitrogen atmosphere or inert atmosphere, and the reaction system is heated to 40°C to 60°C for 5h to 12h to obtain acyl Chlorinated diethylene glycol monoallyl ether carboxylate;

在乙醇胺、N’N-二甲基甲酰胺中和季铵盐化合物混合物中加入所得的酰氯化二乙二醇单烯丙基醚羧酸酯,于65℃~90℃下反应为5~24h,得到封端季铵盐二乙二醇单烯丙基醚羧酸酯,即制得季铵盐聚醚酯单体。The obtained acyl chloride diethylene glycol monoallyl ether carboxylate is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the reaction is carried out at 65°C to 90°C for 5 to 24 hours to obtain a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, that is, a quaternary ammonium salt polyether ester monomer is obtained.

在一实施例中,所述氨基酸为谷氨酸、天冬氨酸中的一种或多种组合;所述溶剂A为二氯甲烷、三氯甲烷、乙腈、甲苯中的一种或多种组合;所述第二催化剂为氯化亚砜、硫酸铜、钛酸四丁酯中的一种或多种组合;所述不饱和酸酐为马来酸酐、丁二酸酐中的一种或多种组合;所述季铵盐化合物为氯化铵、甲基丙烯酰氧乙基三甲基氯化铵、二甲基烷基氯化铵、苄基三甲基氯化铵、矮壮素中的一种或多种组合。In one embodiment, the amino acid is one or more combinations of glutamic acid and aspartic acid; the solvent A is one or more combinations of dichloromethane, chloroform, acetonitrile, and toluene; the second catalyst is one or more combinations of thionyl chloride, copper sulfate, and tetrabutyl titanate; the unsaturated acid anhydride is one or more combinations of maleic anhydride and succinic anhydride; the quaternary ammonium salt compound is one or more combinations of ammonium chloride, methacryloyloxyethyltrimethylammonium chloride, dimethylalkylammonium chloride, benzyltrimethylammonium chloride, and chlormequat.

本发明还提供一种如上所述的EPEG型聚羧酸减水剂的制备方法,其包括以下步骤:The present invention also provides a method for preparing the EPEG type polycarboxylate water reducer as described above, which comprises the following steps:

将乙二醇单乙烯基聚乙二醇醚溶解于水中;在乙二醇单乙烯基聚乙二醇醚水溶液中加入不饱和酰胺单体、硫酸盐、硅烷单体、氯化烯丙基磷酸二甲酯和氧化剂制得底液,并控制反应体系温度为10℃~15℃;Dissolving ethylene glycol monovinyl polyethylene glycol ether in water; adding unsaturated amide monomer, sulfate, silane monomer, dimethyl chloroallyl phosphate and oxidant to the aqueous solution of ethylene glycol monovinyl polyethylene glycol ether to prepare a base solution, and controlling the temperature of the reaction system to be 10° C. to 15° C.;

在底液中加入不饱和羧酸单体、季铵盐聚醚酯单体、不饱和磺酸盐、链转移剂以及还原剂,在10℃~15℃下进行共聚反应,制得所述EPEG型聚羧酸减水剂。Unsaturated carboxylic acid monomer, quaternary ammonium salt polyether ester monomer, unsaturated sulfonate, chain transfer agent and reducing agent are added to the base liquid, and copolymerization reaction is carried out at 10° C. to 15° C. to prepare the EPEG type polycarboxylate water reducer.

本发明还提供一种季铵盐聚醚酯单体,其制备方法如下:The present invention also provides a quaternary ammonium salt polyether ester monomer, and the preparation method thereof is as follows:

将二乙二醇单烯丙基醚、氨基酸、第二催化剂加入到反应釜内混合均匀,于60℃~120℃下反应2~8h后冷至室温,再将三氯甲烷加入到反应釜内混匀并静置12~24h后,即得二乙二醇单烯丙基醚羧酸酯;Add diethylene glycol monoallyl ether, amino acid and the second catalyst into a reaction kettle and mix them evenly, react at 60°C to 120°C for 2 to 8 hours and then cool to room temperature, then add chloroform into the reaction kettle, mix evenly and let stand for 12 to 24 hours to obtain diethylene glycol monoallyl ether carboxylate;

将所得的二乙二醇单烯丙基醚羧酸酯,加入不饱和酸酐和溶剂A内溶解,而后加入吡啶进行反应,得到端羧基二乙二醇单烯丙基醚羧酸酯;The obtained diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A to dissolve, and then pyridine is added to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate;

将所得的端羧基二乙二醇单烯丙基醚羧酸酯溶解到N’N-二甲基甲酰胺中,在氮气气氛或惰性气氛下加入氯化亚砜,将反应体系升温至40℃~60℃反应5h~12h,制得酰氯化二乙二醇单烯丙基醚羧酸酯; The obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under a nitrogen atmosphere or an inert atmosphere, and the reaction system is heated to 40°C to 60°C for 5h to 12h to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

在乙醇胺、N’N-二甲基甲酰胺中和季铵盐化合物混合物中加入所得的酰氯化二乙二醇单烯丙基醚羧酸酯,于65℃~90℃下反应为5~24h,制得季铵盐聚醚酯单体。The obtained diethylene glycol monoallyl ether carboxylate acylation is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the mixture is reacted at 65°C to 90°C for 5 to 24 hours to obtain a quaternary ammonium salt polyether ester monomer.

基于上述,与现有技术相比,本发明提供的EPEG型聚羧酸减水剂,具有以下有益效果:Based on the above, compared with the prior art, the EPEG type polycarboxylate water reducer provided by the present invention has the following beneficial effects:

本发明提供的EPEG型聚羧酸减水剂,其能够有效降低混凝土粘度,改善混凝土的和易性及流速,且其对混凝土的力学性能有提升作用;其具有掺量低、减水率高、和易性好、能够显著降低浆体粘度等优点。The EPEG type polycarboxylate water-reducing agent provided by the present invention can effectively reduce the viscosity of concrete, improve the workability and flow rate of concrete, and improve the mechanical properties of concrete; it has the advantages of low dosage, high water reduction rate, good workability, and can significantly reduce the viscosity of slurry.

本发明的其它特征和有益效果将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。本发明的目的和其他有益效果可通过在说明书、权利要求书中所特别指出的结构来实现和获得。Other features and beneficial effects of the present invention will be described in the following description, and partly become apparent from the description, or understood by practicing the present invention. The purpose and other beneficial effects of the present invention can be achieved and obtained by the structures specifically pointed out in the description and claims.

具体实施方式Detailed ways

为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例;下面所描述的本发明不同实施方式中所设计的技术特征只要彼此之间未构成冲突就可以相互结合;基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are part of the embodiments of the present invention, not all of the embodiments; the technical features designed in the different implementation modes of the present invention described below can be combined with each other as long as they do not conflict with each other; based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative work are within the scope of protection of the present invention.

在本发明的描述中,需要说明的是,本发明所使用的所有术语(包括技术术语和科学术语)具有与本发明所属领域的普通技术人员通常所理解的含义相同的含义,不能理解为对本发明的限制;应进一步理解,本发明所使用的术语应被理解为具有与这些术语在本说明书的上下文和相关领域中的含义一致的含义,并且不应以理想化或过于正式的意义来理解,除本发明中明确如此定义之外。In the description of the present invention, it should be noted that all terms used in the present invention (including technical terms and scientific terms) have the same meanings as those generally understood by ordinary technicians in the field to which the present invention belongs, and should not be understood as limitations on the present invention; it should be further understood that the terms used in the present invention should be understood to have the same meanings as these terms in the context of this specification and in the relevant fields, and should not be understood in an idealized or overly formal sense, unless explicitly defined in this invention.

本发明提供该EPEG型聚羧酸减水剂的制备方法的优选实施方案,具体包括如下步骤:The present invention provides a preferred embodiment of the preparation method of the EPEG type polycarboxylate water reducer, which specifically comprises the following steps:

步骤a)将乙二醇单乙烯基聚乙二醇醚(EPEG)溶解于水中,放入反应器中,充分搅 拌均匀;Step a) dissolving ethylene glycol monovinyl polyethylene glycol ether (EPEG) in water, placing in a reactor, and stirring thoroughly. Mix well;

步骤b)往步骤a的乙二醇单乙烯基聚乙二醇醚水溶液中加入不饱和酰胺单体、硫酸盐、硅烷单体、氯化烯丙基磷酸二甲酯和氧化剂制得底液,控制温度为10℃~15℃;Step b) adding unsaturated amide monomer, sulfate, silane monomer, dimethyl chloroallyl phosphate and oxidant to the aqueous solution of ethylene glycol monovinyl polyglycol ether in step a to prepare a base solution, and controlling the temperature to be 10° C. to 15° C.;

步骤c)将不饱和羧酸单体、季铵盐聚醚酯单体与水配成A溶液,并滴加入底液中,滴加时间为50~80min;将不饱和磺酸盐、链转移剂和水配成溶液C液,并滴加入底液中,滴加时间为50~80min;将还原剂与水配成B溶液,并滴加入底液中,滴加时间60~80min;滴加过程中,反应体系在10℃~15℃下进行共聚反应,滴加结束后继续保温1~2h,最后加入液碱中和,制得所述EPEG型聚羧酸减水剂。Step c) unsaturated carboxylic acid monomer, quaternary ammonium salt polyether ester monomer and water are prepared into solution A, and the solution is added dropwise to the base liquid for 50 to 80 minutes; unsaturated sulfonate, chain transfer agent and water are prepared into solution C, and the solution is added dropwise to the base liquid for 50 to 80 minutes; reducing agent and water are prepared into solution B, and the solution is added dropwise to the base liquid for 60 to 80 minutes; during the dropping process, the reaction system is copolymerized at 10° C. to 15° C., and the temperature is kept for 1 to 2 hours after the dropping is completed, and finally liquid alkali is added for neutralization to obtain the EPEG type polycarboxylate water reducer.

按重量份计,共聚反应体系中的原料包括所述乙二醇单乙烯基聚乙二醇醚200~300份、不饱和酰胺单体4~8份,不饱和羧酸单体20~30份,不饱和磺酸盐4~8份,硅烷单体2~4份,氯化烯丙基磷酸二甲酯4~6份,季铵盐聚醚酯单体4~6份,氧化剂2.5~4.5份,还原剂0.2~0.4份,链转移剂1~1.5份,硫酸盐1~2份,水350~400份。其中,整体酸醚比为1.0~2.0。By weight, the raw materials in the copolymerization reaction system include 200-300 parts of ethylene glycol monovinyl polyethylene glycol ether, 4-8 parts of unsaturated amide monomers, 20-30 parts of unsaturated carboxylic acid monomers, 4-8 parts of unsaturated sulfonates, 2-4 parts of silane monomers, 4-6 parts of dimethyl chloroallyl phosphate, 4-6 parts of quaternary ammonium salt polyether ester monomers, 2.5-4.5 parts of oxidants, 0.2-0.4 parts of reducing agents, 1-1.5 parts of chain transfer agents, 1-2 parts of sulfates, and 350-400 parts of water. The overall acid-ether ratio is 1.0-2.0.

(1)对于氯化烯丙基磷酸二甲酯,本发明还提供其制备方法的优选实施方案如下:(1) For chloroallyl dimethyl phosphate, the present invention also provides a preferred embodiment of its preparation method as follows:

所述氯化烯丙基磷酸二甲酯由烯丙基磷酸二甲酯与氯化亚砜进行酯化反应制得;具体过程为:The chlorinated allyl dimethyl phosphate is prepared by esterification reaction of allyl dimethyl phosphate and thionyl chloride; the specific process is:

将烯丙基磷酸二甲酯和溶剂A在室温下搅拌0.5~2h混合;并加入第一催化剂和阻聚剂,反应体系升温至40℃~60℃,在此温度下滴加氯化亚砜酯化反应2~4h并保温3~5h,反应结束后过滤、旋蒸处理后制得所述氯化烯丙基磷酸二甲酯;其中,所述氯化烯丙基磷酸二甲酯的制备全程在氮气气氛或惰性气氛下进行反应;Allyl dimethyl phosphate and solvent A are stirred at room temperature for 0.5 to 2 hours to mix; and a first catalyst and a polymerization inhibitor are added, the reaction system is heated to 40°C to 60°C, thionyl chloride is added dropwise at this temperature for esterification reaction for 2 to 4 hours and kept warm for 3 to 5 hours, and after the reaction is completed, the allyl dimethyl phosphate is filtered and subjected to rotary evaporation to obtain the allyl dimethyl phosphate; wherein the preparation of the allyl dimethyl phosphate is carried out under a nitrogen atmosphere or an inert atmosphere throughout the reaction;

所述烯丙基磷酸二甲酯、溶剂A、氯化亚砜、第一催化剂与阻聚剂的重量比为100:(350~400):(100~150):(5~10):(0.5~1.0)。The weight ratio of allyl dimethyl phosphate, solvent A, thionyl chloride, the first catalyst and the polymerization inhibitor is 100: (350-400): (100-150): (5-10): (0.5-1.0).

其中,所述溶剂A可优选二氯甲烷、三氯甲烷、乙腈、甲苯中的一种或多种组合;所述第一催化剂可优选N’N二甲基甲酰胺、吡啶、4-二甲氨基吡啶、浓硫酸、乙基磺酸中 的一种或多种组合;所述阻聚剂可优选对苯二酚、对羟基苯甲醚、吩噻嗪、氯化亚铜、氯化铁中的一种或多种组合。The solvent A may be preferably one or more of dichloromethane, chloroform, acetonitrile, and toluene; the first catalyst may be preferably N'N-dimethylformamide, pyridine, 4-dimethylaminopyridine, concentrated sulfuric acid, ethylsulfonic acid, One or more combinations of; the inhibitor may preferably be one or more combinations of hydroquinone, p-hydroxyanisole, phenothiazine, cuprous chloride, and ferric chloride.

(2)对于季铵盐聚醚酯单体,本发明还提供季铵盐聚醚酯单体的制备方法的优选实施方案如下:(2) For the quaternary ammonium salt polyether ester monomer, the present invention also provides a preferred embodiment of the preparation method of the quaternary ammonium salt polyether ester monomer as follows:

室温下,将二乙二醇单烯丙基醚、氨基酸、第二催化剂加入到反应釜内搅拌混合均匀,于60℃~120℃下反应2~8h后冷至室温,再将三氯甲烷加入到反应釜内混匀并静置12~24h后,过滤,滤液在50℃~65℃下减压蒸除三氯甲烷,即分离得到二乙二醇单烯丙基醚羧酸酯;其中,所述二乙二醇单烯丙基醚与三氯甲烷的重量比为1:(1~3);At room temperature, diethylene glycol monoallyl ether, amino acid and a second catalyst are added to a reaction kettle and stirred to mix evenly, reacted at 60°C to 120°C for 2 to 8 hours and then cooled to room temperature, and then chloroform is added to the reaction kettle and mixed evenly and allowed to stand for 12 to 24 hours, filtered, and the filtrate is evaporated under reduced pressure at 50°C to 65°C to remove chloroform, thereby separating and obtaining diethylene glycol monoallyl ether carboxylate; wherein the weight ratio of diethylene glycol monoallyl ether to chloroform is 1:(1 to 3);

将所得的二乙二醇单烯丙基醚羧酸酯,加入不饱和酸酐和溶剂A内搅拌溶解,而后滴加吡啶进行反应,得到端羧基二乙二醇单烯丙基醚羧酸酯;其中,反应温度控制在(40℃~60℃);The obtained diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A, stirred and dissolved, and then pyridine is added dropwise to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate; wherein the reaction temperature is controlled at (40° C. to 60° C.);

将所得的端羧基二乙二醇单烯丙基醚羧酸酯溶解到N’N-二甲基甲酰胺中,在氮气气氛或惰性气氛下加入氯化亚砜,将反应体系升温至40℃~60℃反应5h~12h,减压浓缩除去氯化亚砜,乙醚洗涤产物,制得酰氯化二乙二醇单烯丙基醚羧酸酯;The obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under a nitrogen atmosphere or an inert atmosphere, the reaction system is heated to 40°C to 60°C for 5h to 12h, the thionyl chloride is removed by concentration under reduced pressure, and the product is washed with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

在乙醇胺、N’N-二甲基甲酰胺中和季铵盐化合物混合物中加入所得的酰氯化二乙二醇单烯丙基醚羧酸酯,于65℃~90℃下反应为5~24h,反应液经分离纯化后,得到封端季铵盐二乙二醇单烯丙基醚羧酸酯,即得季铵盐聚醚酯单体。The obtained acyl chloride diethylene glycol monoallyl ether carboxylate is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the reaction is carried out at 65°C to 90°C for 5 to 24 hours. After separation and purification of the reaction liquid, a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate is obtained, i.e., a quaternary ammonium salt polyether ester monomer is obtained.

二乙二醇单烯丙基醚、氨基酸、不饱和酸酐、氯化亚砜、季铵盐化合物的重量比(100~200):(65~130):(60~120):(200~400):(2~6);The weight ratio of diethylene glycol monoallyl ether, amino acid, unsaturated acid anhydride, thionyl chloride and quaternary ammonium salt compound is (100-200): (65-130): (60-120): (200-400): (2-6);

其中,所述氨基酸可优选谷氨酸、天冬氨酸中的一种或多种组合;所述溶剂A可优选二氯甲烷、三氯甲烷、乙腈和甲苯中的一种或多种组合;所述第二催化剂可优选氯化亚砜、硫酸铜、钛酸四丁酯中的一种或多种组合;所述不饱和酸酐优选马来酸酐、丁二酸酐中的一种或多种组合;所述季铵盐化合物优选氯化铵、甲基丙烯酰氧乙基三甲基氯化铵、二甲基烷基氯化铵、苄基三甲基氯化铵、矮壮素中的一种或多种组合。进一步优选地,氨基酸 选用天冬氨酸;所述溶剂A选用三氯甲烷;第二催化剂选用硫酸铜;不饱和酸酐选用丁二酸酐;季铵盐化合物选用二甲基烷基氯化铵。Among them, the amino acid can be preferably one or more combinations of glutamic acid and aspartic acid; the solvent A can be preferably one or more combinations of dichloromethane, chloroform, acetonitrile and toluene; the second catalyst can be preferably one or more combinations of thionyl chloride, copper sulfate and tetrabutyl titanate; the unsaturated acid anhydride can be preferably one or more combinations of maleic anhydride and succinic anhydride; the quaternary ammonium salt compound can be preferably one or more combinations of ammonium chloride, methacryloyloxyethyl trimethylammonium chloride, dimethyl alkyl ammonium chloride, benzyl trimethyl ammonium chloride and chlormequat. More preferably, the amino acid Aspartic acid is selected; the solvent A is chloroform; the second catalyst is copper sulfate; the unsaturated acid anhydride is succinic anhydride; and the quaternary ammonium salt compound is dimethyl alkyl ammonium chloride.

(3)对于其他共聚单体:(3) For other comonomers:

所述不饱和酰胺单体可优选丙烯酰胺、N-(2-二甲氨基乙基)丙烯酰胺、N,N-亚甲基双丙烯酰胺、环丙酰胺、己内酰胺中的一种或多种组合;所述不饱和羧酸单体可优选丙烯酸、甲基丙烯酸、富马酸、马来酸酐、衣康酸中的一种或多种组合;所述不饱和磺酸盐可优选甲基丙烯磺酸钠、苯乙烯磺酸钠、2-丙烯酰胺-2-甲基丙磺酸、十二烷基苯磺酸钠中的一种或多种组合;所述硅烷单体可优选乙烯基三甲氧基硅烷、乙烯基三乙氧硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、KH550、KH570中的一种或多种组合。The unsaturated amide monomer may preferably be one or more combinations of acrylamide, N-(2-dimethylaminoethyl)acrylamide, N,N-methylenebisacrylamide, cyclopropaneamide, and caprolactam; the unsaturated carboxylic acid monomer may preferably be one or more combinations of acrylic acid, methacrylic acid, fumaric acid, maleic anhydride, and itaconic acid; the unsaturated sulfonate may preferably be one or more combinations of sodium methyl propylene sulfonate, sodium styrene sulfonate, 2-acrylamide-2-methylpropane sulfonic acid, and sodium dodecylbenzene sulfonate; the silane monomer may preferably be one or more combinations of vinyl trimethoxy silane, vinyl triethoxy silane, γ-methacryloxypropyl trimethoxy silane, KH550, and KH570.

(4)对于其他共聚反应原料:(4) For other copolymerization raw materials:

步骤a)中,还原剂优选亚硫酸钠、吊白块、亚硫酸氢钠、次磷酸钠中的一种或多种组合,其中,次磷酸钠同时能作为链转移剂使用;氧化剂可优选过氧化氢、过氧化钠、过氧化钾、过氧化镁、过硫酸钠、过硫酸铵、重铬酸钠、重铬酸钾、高锰酸钾中的一种或多种组合;链转移剂可优选硫代乙醇酸、次磷酸钠、磷酸三钠、巯基丙酸、巯基乙醇、巯基乙酸的一种或多种组合。步骤b)中,硫酸盐优选硫酸亚铁。进一步优选地,所述硅烷单体为KH550;不饱和羧酸单体为丙烯酸;氧化剂为过氧化氢。In step a), the reducing agent is preferably one or more combinations of sodium sulfite, bleaching powder, sodium bisulfite, and sodium hypophosphite, wherein sodium hypophosphite can also be used as a chain transfer agent; the oxidizing agent may be preferably one or more combinations of hydrogen peroxide, sodium peroxide, potassium peroxide, magnesium peroxide, sodium persulfate, ammonium persulfate, sodium dichromate, potassium dichromate, and potassium permanganate; the chain transfer agent may be preferably one or more combinations of thioglycolic acid, sodium hypophosphite, trisodium phosphate, mercaptopropionic acid, mercaptoethanol, and thioglycolic acid. In step b), the sulfate is preferably ferrous sulfate. Further preferably, the silane monomer is KH550; the unsaturated carboxylic acid monomer is acrylic acid; and the oxidizing agent is hydrogen peroxide.

本发明还提供如下所示实施例和对比例:The present invention also provides the following embodiments and comparative examples:

实施例1Example 1

(1)制备氯化烯丙基磷酸二甲酯A:(1) Preparation of allyl dimethyl phosphate A:

将100g烯丙基磷酸二甲酯、350g二氯甲烷溶剂投入四口烧瓶装置中,搅拌均匀后,加入5g催化剂DMF和0.5g阻聚剂吩噻嗪。然后在搅拌过程中升温至45℃,并在该温度下滴加125g氯化亚砜,滴加时间约为3h,并在冷凝回流中保温4h,全程均在氮气气氛中反应。应结束后过滤、旋蒸处理后制备可得氯化烯丙基磷酸二甲酯A。100g of allyl dimethyl phosphate and 350g of dichloromethane solvent were put into a four-necked flask, stirred evenly, and then 5g of catalyst DMF and 0.5g of inhibitor phenothiazine were added. Then the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and kept warm for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate A.

(2)制备封端季铵盐二乙二醇单烯丙基醚羧酸酯,即季铵盐聚醚酯单体: (2) Preparation of blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, i.e., quaternary ammonium salt polyether ester monomer:

步骤a)将100g二乙二醇单烯丙基醚分子量为1200、67g L-天冬氨酸和0.85g催化剂(硫酸铜)加入反应釜中,搅拌均匀,放置于100℃下反应6h后冷却到室温,之后在将250ml三氯甲烷加入反应釜中,搅拌均匀后静置12h后后过滤,滤液在60℃下减压蒸除三氯甲烷,即得二乙二醇单烯丙基醚天冬氨酸酯;Step a) 100g of diethylene glycol monoallyl ether with a molecular weight of 1200, 67g of L-aspartic acid and 0.85g of a catalyst (copper sulfate) are added to a reactor, stirred evenly, placed at 100°C for reaction for 6 hours and then cooled to room temperature, then 250ml of chloroform is added to the reactor, stirred evenly and allowed to stand for 12 hours and then filtered, and the filtrate is evaporated under reduced pressure at 60°C to remove chloroform, thereby obtaining diethylene glycol monoallyl ether aspartic acid ester;

步骤b)将100g二乙二醇单烯丙基醚羧酸酯和60g丁二酸酐加入300三氯甲烷中搅拌溶解后,升温至60℃,并且在该温度下滴加15g吡啶,滴加时间为3h,反应后加入三氯甲烷和饱和碳酸氢钠溶液萃取,将有机相干燥后用乙醚洗涤,得到端羧基二乙二醇单烯丙基醚羧酸酯,然后溶解到N,N-二甲基甲酰胺中,在氮气氛围中滴加200mL的氯化亚砜,升温至60℃反应8h,减压浓缩除去氯化亚砜,乙醚洗涤产物,得到酰氯化二乙二醇单烯丙基醚羧酸酯;Step b) adding 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride to 300ml of chloroform and stirring to dissolve, heating to 60°C, and adding 15g of pyridine dropwise at the same temperature for 3h, adding chloroform and saturated sodium bicarbonate solution for extraction after the reaction, drying the organic phase and washing with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, then dissolving it in N,N-dimethylformamide, adding 200mL of thionyl chloride dropwise in a nitrogen atmosphere, heating to 60°C for reaction for 8h, concentrating under reduced pressure to remove thionyl chloride, and washing the product with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

步骤c)将100g酰氯化二乙二醇单烯丙基醚羧酸酯加入四口烧瓶中,在加入100ml的DMF溶液重复溶解之后,升温至80℃加入5.8g乙醇胺,冷凝回流12h,之后将2.2g二甲基烷基氯化铵和20ml的DMF溶液滴加1h后,冷凝回流12h,全程均在氮气氛围下进行。反应结束后,将反应产物进行抽滤和旋蒸制备封端季铵盐二乙二醇单烯丙基醚羧酸酯。Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.

(3)制备EPEG型聚羧酸减水剂:(3) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,1g次磷酸钠,4g氯化烯丙基磷酸二甲酯A搅匀后调节温度在10~15℃区间,备用。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water into a four-necked flask, stir to dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration is 1%), 2g of KH550, 1g of sodium hypophosphite, and 4g of dimethyl chloroallyl phosphate A, stir well, adjust the temperature to 10-15°C, and set aside.

将20g丙烯酸、4g季铵盐聚醚酯单体和30g水配成A液;将4g AMPS、0.8g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。 20g acrylic acid, 4g quaternary ammonium salt polyether ester monomer and 30g water are prepared into liquid A; 4g AMPS, 0.8g mercaptopropionic acid monomer and 50g water are prepared into liquid B; 0.25g bleaching powder and 50g water are prepared into liquid C. Before adding, 2.5g hydrogen peroxide is added to a four-necked flask and stirred for 5 minutes before adding simultaneously, wherein liquids A and B are added for 50min, and liquid C is added for 60min; after the addition is completed, the temperature is kept for 1h, and the temperature does not exceed 25℃ throughout the process. After the insulation is completed, liquid is added to adjust the pH value of the solution to 5.0-6.5, and an EPEG type polycarboxylic acid water reducer is obtained.

实施例2Example 2

(1)制备氯化烯丙基磷酸二甲酯B:(1) Preparation of allyl dimethyl phosphate B:

将100g烯丙基磷酸二甲酯、300g二氯甲烷和50g乙腈溶剂投入四口烧瓶装置中,搅拌均匀后,加入催化剂4gDMF和1.5g吡啶和阻聚剂0.3g吩噻嗪和0.25g氯化亚铁。然后在搅拌过程中升温至45℃,并在该温度下滴加125g氯化亚砜,滴加时间约为3h,并在冷凝回流中保温4h,全程均在氮气气氛中反应。应结束后过滤、旋蒸处理后制备可得氯化烯丙基磷酸二甲酯B。100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.

(2)制备封端季铵盐二乙二醇单烯丙基醚羧酸酯,即季铵盐聚醚酯单体:(2) Preparation of blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, i.e., quaternary ammonium salt polyether ester monomer:

步骤a)将100g二乙二醇单烯丙基醚分子量为1200、67g L-天冬氨酸和0.85g催化剂(硫酸铜)加入反应釜中,搅拌均匀,放置于100℃下反应6h后冷却到室温,之后在将250m三氯甲烷加入反应釜中,搅拌均匀后静置12h后后过滤,滤液在60℃下减压蒸除三氯甲烷,即得二乙二醇单烯丙基醚天冬氨酸酯;Step a) 100g of diethylene glycol monoallyl ether with a molecular weight of 1200, 67g of L-aspartic acid and 0.85g of a catalyst (copper sulfate) are added to a reactor, stirred evenly, placed at 100°C for reaction for 6 hours and then cooled to room temperature, then 250ml of chloroform is added to the reactor, stirred evenly and allowed to stand for 12 hours and then filtered, and the filtrate is evaporated under reduced pressure at 60°C to remove chloroform, thereby obtaining diethylene glycol monoallyl ether aspartic acid ester;

步骤b)将100g二乙二醇单烯丙基醚羧酸酯和60g丁二酸酐加入300三氯甲烷中搅拌溶解后,升温至60℃,并且在该温度下滴加15g吡啶,滴加时间为3h,反应后加入三氯甲烷和饱和碳酸氢钠溶液萃取,将有机相干燥后用乙醚洗涤,得到端羧基二乙二醇单烯丙基醚羧酸酯,然后溶解到N,N-二甲基甲酰胺中,在氮气氛围中滴加200mL的氯化亚砜,升温至60℃反应8h,减压浓缩除去氯化亚砜,乙醚洗涤产物,得到酰氯化二乙二醇单烯丙基醚羧酸酯;Step b) adding 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride to 300ml of chloroform and stirring to dissolve, heating to 60°C, and adding 15g of pyridine dropwise at the same temperature for 3h, adding chloroform and saturated sodium bicarbonate solution for extraction after the reaction, drying the organic phase and washing with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, then dissolving it in N,N-dimethylformamide, adding 200mL of thionyl chloride dropwise in a nitrogen atmosphere, heating to 60°C for reaction for 8h, concentrating under reduced pressure to remove thionyl chloride, and washing the product with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

步骤c)将100g酰氯化二乙二醇单烯丙基醚羧酸酯加入四口烧瓶中,在加入100ml的DMF溶液重复溶解之后,升温至80℃加入5.8g乙醇胺,冷凝回流12h,之后将2.2g二甲基烷基氯化铵和20ml的DMF溶液滴加1h后,冷凝回流12h,全程均在氮气氛围下进行。反应结束后,将反应产物进行抽滤和旋蒸制备封端季铵盐二乙二醇单烯丙基醚羧酸酯。Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.

(3)制备EPEG型聚羧酸减水剂: (3) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,1g次磷酸钠,4g氯化烯丙基磷酸二甲酯B搅匀后调节温度在10~15℃区间,备用。将20g丙烯酸、4g季铵盐聚醚酯单体和30g水配成A液;将4g AMPS、0.8g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water to a four-necked flask, stir and dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration of 1%), 2g of KH550, 1g of sodium hypophosphite, and 4g of dimethyl chloroallyl phosphate B, stir well, adjust the temperature to 10-15°C, and set aside. Prepare liquid A by mixing 20g of acrylic acid, 4g of quaternary ammonium salt polyether ester monomer, and 30g of water; prepare liquid B by mixing 4g of AMPS, 0.8g of mercaptopropionic acid monomer, and 50g of water; prepare liquid C by mixing 0.25g of bleaching powder and 50g of water. Before adding, add 2.5g of hydrogen peroxide to a four-necked flask, stir for 5 minutes, and then start adding simultaneously, with liquids A and B added for 50min, and liquid C added for 60min; keep warm for 1h after the addition is completed, and the temperature does not exceed 25°C throughout the process. After the heat preservation is completed, liquid is added to adjust the pH value of the solution to be controlled at 5.0-6.5 to obtain an EPEG type polycarboxylate water reducer.

实施例3Example 3

(1)制备氯化烯丙基磷酸二甲酯B:(1) Preparation of allyl dimethyl phosphate B:

将100g烯丙基磷酸二甲酯、300g二氯甲烷和50g乙腈溶剂投入四口烧瓶装置中,搅拌均匀后,加入催化剂4gDMF和1.5g吡啶和阻聚剂0.3g吩噻嗪和0.25g氯化亚铁。然后在搅拌过程中升温至45℃,并在该温度下滴加125g氯化亚砜,滴加时间约为3h,并在冷凝回流中保温4h,全程均在氮气气氛中反应。应结束后过滤、旋蒸处理后制备可得氯化烯丙基磷酸二甲酯B。100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.

(2)制备封端季铵盐二乙二醇单烯丙基醚羧酸酯,即季铵盐聚醚酯单体:(2) Preparation of blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, i.e., quaternary ammonium salt polyether ester monomer:

步骤a)将100g二乙二醇单烯丙基醚分子量为1200、67g L-天冬氨酸和0.85g催化剂(硫酸铜)加入反应釜中,搅拌均匀,放置于100℃下反应6h后冷却到室温,之后在将250m三氯甲烷加入反应釜中,搅拌均匀后静置12h后后过滤,滤液在60℃下减压蒸除三氯甲烷,即得二乙二醇单烯丙基醚天冬氨酸酯;Step a) 100g of diethylene glycol monoallyl ether with a molecular weight of 1200, 67g of L-aspartic acid and 0.85g of a catalyst (copper sulfate) are added to a reactor, stirred evenly, placed at 100°C for reaction for 6 hours and then cooled to room temperature, then 250ml of chloroform is added to the reactor, stirred evenly and allowed to stand for 12 hours and then filtered, and the filtrate is evaporated under reduced pressure at 60°C to remove chloroform, thereby obtaining diethylene glycol monoallyl ether aspartic acid ester;

步骤b)将100g二乙二醇单烯丙基醚羧酸酯和60g丁二酸酐加入300三氯甲烷中搅拌溶解后,升温至60℃,并且在该温度下滴加15g吡啶,滴加时间为3h,反应后加入三氯甲烷和饱和碳酸氢钠溶液萃取,将有机相干燥后用乙醚洗涤,得到端羧基二乙二醇单烯丙基醚羧酸酯,然后溶解到N,N-二甲基甲酰胺中,在氮气氛围中滴加200mL的氯化亚 砜,升温至60℃反应8h,减压浓缩除去氯化亚砜,乙醚洗涤产物,得到酰氯化二乙二醇单烯丙基醚羧酸酯;Step b) 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride were added to 300ml of chloroform and stirred to dissolve, and then the temperature was raised to 60°C, and 15g of pyridine was added dropwise at this temperature for 3h. After the reaction, chloroform and saturated sodium bicarbonate solution were added for extraction, and the organic phase was dried and washed with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, which was then dissolved in N,N-dimethylformamide, and 200mL of chlorinated amine was added dropwise in a nitrogen atmosphere. sulfone, heating to 60°C for 8h, concentrating under reduced pressure to remove thionyl chloride, washing the product with ether to obtain diethylene glycol monoallyl ether carboxylate;

步骤c)将100g酰氯化二乙二醇单烯丙基醚羧酸酯加入四口烧瓶中,在加入100ml的DMF溶液重复溶解之后,升温至80℃加入5.8g乙醇胺,冷凝回流12h,之后将2.2g二甲基烷基氯化铵和20ml的DMF溶液滴加1h后,冷凝回流12h,全程均在氮气氛围下进行。反应结束后,将反应产物进行抽滤和旋蒸制备封端季铵盐二乙二醇单烯丙基醚羧酸酯。Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.

(3)制备EPEG型聚羧酸减水剂:(3) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、1g次磷酸钠,4g氯化烯丙基磷酸二甲酯B搅匀后调节温度在10~15℃区间,备用。将20g丙烯酸、4g季铵盐聚醚酯单体和30g水配成A液;将4g AMPS、0.8g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water to a four-necked flask, stir and dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration of 1%), 1g of sodium hypophosphite, and 4g of dimethyl chloroallyl phosphate B, stir well, adjust the temperature to 10-15℃, and set aside. Prepare 20g of acrylic acid, 4g of quaternary ammonium salt polyether ester monomer and 30g of water to make liquid A; prepare 4g of AMPS, 0.8g of mercaptopropionic acid monomer and 50g of water to make liquid B; prepare 0.25g of bleaching powder and 50g of water to make liquid C. Before adding, add 2.5g of hydrogen peroxide to a four-necked flask, stir for 5 minutes, and then start to add simultaneously, wherein liquids A and B are added for 50min, and liquid C is added for 60min; after the addition is completed, keep warm for 1h, and the temperature does not exceed 25℃ throughout the process. After the insulation is completed, add liquid to adjust the pH value of the solution to 5.0-6.5 to obtain EPEG type polycarboxylic acid water reducer.

实施例4Example 4

(1)制备氯化烯丙基磷酸二甲酯B:(1) Preparation of allyl dimethyl phosphate B:

将100g烯丙基磷酸二甲酯、300g二氯甲烷和50g乙腈溶剂投入四口烧瓶装置中,搅拌均匀后,加入催化剂4gDMF和1.5g吡啶和阻聚剂0.3g吩噻嗪和0.25g氯化亚铁。然后在搅拌过程中升温至45℃,并在该温度下滴加125g氯化亚砜,滴加时间约为3h,并在冷凝回流中保温4h,全程均在氮气气氛中反应。应结束后过滤、旋蒸处理后制备可得氯化烯丙基磷酸二甲酯B。100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.

(2)制备封端季铵盐二乙二醇单烯丙基醚羧酸酯,即季铵盐聚醚酯单体: (2) Preparation of blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, i.e., quaternary ammonium salt polyether ester monomer:

步骤a)将100g二乙二醇单烯丙基醚分子量为1200、67g L-天冬氨酸和0.85g催化剂(硫酸铜)加入反应釜中,搅拌均匀,放置于100℃下反应6h后冷却到室温,之后在将250m三氯甲烷加入反应釜中,搅拌均匀后静置12h后后过滤,滤液在60℃下减压蒸除三氯甲烷,即得二乙二醇单烯丙基醚天冬氨酸酯;Step a) 100g of diethylene glycol monoallyl ether with a molecular weight of 1200, 67g of L-aspartic acid and 0.85g of a catalyst (copper sulfate) are added to a reactor, stirred evenly, placed at 100°C for reaction for 6 hours and then cooled to room temperature, then 250ml of chloroform is added to the reactor, stirred evenly and allowed to stand for 12 hours and then filtered, and the filtrate is evaporated under reduced pressure at 60°C to remove chloroform, thereby obtaining diethylene glycol monoallyl ether aspartic acid ester;

步骤b)将100g二乙二醇单烯丙基醚羧酸酯和60g丁二酸酐加入300三氯甲烷中搅拌溶解后,升温至60℃,并且在该温度下滴加15g吡啶,滴加时间为3h,反应后加入三氯甲烷和饱和碳酸氢钠溶液萃取,将有机相干燥后用乙醚洗涤,得到端羧基二乙二醇单烯丙基醚羧酸酯,然后溶解到N,N-二甲基甲酰胺中,在氮气氛围中滴加200mL的氯化亚砜,升温至60℃反应8h,减压浓缩除去氯化亚砜,乙醚洗涤产物,得到酰氯化二乙二醇单烯丙基醚羧酸酯;Step b) adding 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride to 300ml of chloroform and stirring to dissolve, heating to 60°C, and adding 15g of pyridine dropwise at the same temperature for 3h, adding chloroform and saturated sodium bicarbonate solution for extraction after the reaction, drying the organic phase and washing with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, then dissolving it in N,N-dimethylformamide, adding 200mL of thionyl chloride dropwise in a nitrogen atmosphere, heating to 60°C for reaction for 8h, concentrating under reduced pressure to remove thionyl chloride, and washing the product with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

步骤c)将100g酰氯化二乙二醇单烯丙基醚羧酸酯加入四口烧瓶中,在加入100ml的DMF溶液重复溶解之后,升温至80℃加入5.8g乙醇胺,冷凝回流12h,之后将2.2g二甲基烷基氯化铵和20ml的DMF溶液滴加1h后,冷凝回流12h,全程均在氮气氛围下进行。反应结束后,将反应产物进行抽滤和旋蒸制备封端季铵盐二乙二醇单烯丙基醚羧酸酯。Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.

(3)制备EPEG型聚羧酸减水剂:(3) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,4g氯化烯丙基磷酸二甲酯B搅匀后调节温度在10~15℃区间,备用。将20g丙烯酸、4g季铵盐聚醚酯单体和30g水配成A液;将4g AMPS、1.2g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。 Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water to a four-necked flask, stir and dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration is 1%), 2g of KH550, and 4g of dimethyl chloroallyl phosphate B, stir well, and adjust the temperature to 10-15°C for use. 20g of acrylic acid, 4g of quaternary ammonium salt polyether ester monomer and 30g of water are prepared into liquid A; 4g of AMPS, 1.2g of mercaptopropionic acid monomer and 50g of water are prepared into liquid B; 0.25g of bleaching powder and 50g of water are prepared into liquid C. Before adding, add 2.5g of hydrogen peroxide to a four-necked flask, stir for 5 minutes, and then start to add simultaneously, wherein liquids A and B are added for 50min, and liquid C is added for 60min; after the addition is completed, keep warm for 1h, and the temperature does not exceed 25°C throughout the process. After the insulation is completed, add liquid to adjust the pH value of the solution to 5.0-6.5 to obtain an EPEG type polycarboxylic acid water reducer.

实施例5Example 5

(1)制备氯化烯丙基磷酸二甲酯B:(1) Preparation of allyl dimethyl phosphate B:

将100g烯丙基磷酸二甲酯、300g二氯甲烷和50g乙腈溶剂投入四口烧瓶装置中,搅拌均匀后,加入催化剂4gDMF和1.5g吡啶和阻聚剂0.3g吩噻嗪和0.25g氯化亚铁。然后在搅拌过程中升温至45℃,并在该温度下滴加125g氯化亚砜,滴加时间约为3h,并在冷凝回流中保温4h,全程均在氮气气氛中反应。应结束后过滤、旋蒸处理后制备可得氯化烯丙基磷酸二甲酯B。100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.

(2)制备封端季铵盐二乙二醇单烯丙基醚羧酸酯,即季铵盐聚醚酯单体:(2) Preparation of blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, i.e., quaternary ammonium salt polyether ester monomer:

步骤a)将100g二乙二醇单烯丙基醚分子量为1200、67g L-天冬氨酸和0.85g催化剂(硫酸铜)加入反应釜中,搅拌均匀,放置于100℃下反应6h后冷却到室温,之后在将250m三氯甲烷加入反应釜中,搅拌均匀后静置12h后后过滤,滤液在60℃下减压蒸除三氯甲烷,即得二乙二醇单烯丙基醚天冬氨酸酯;Step a) 100g of diethylene glycol monoallyl ether with a molecular weight of 1200, 67g of L-aspartic acid and 0.85g of a catalyst (copper sulfate) are added to a reactor, stirred evenly, placed at 100°C for reaction for 6 hours and then cooled to room temperature, then 250ml of chloroform is added to the reactor, stirred evenly and allowed to stand for 12 hours and then filtered, and the filtrate is evaporated under reduced pressure at 60°C to remove chloroform, thereby obtaining diethylene glycol monoallyl ether aspartic acid ester;

步骤b)将100g二乙二醇单烯丙基醚羧酸酯和60g丁二酸酐加入300三氯甲烷中搅拌溶解后,升温至60℃,并且在该温度下滴加15g吡啶,滴加时间为3h,反应后加入三氯甲烷和饱和碳酸氢钠溶液萃取,将有机相干燥后用乙醚洗涤,得到端羧基二乙二醇单烯丙基醚羧酸酯,然后溶解到N,N-二甲基甲酰胺中,在氮气氛围中滴加200mL的氯化亚砜,升温至60℃反应8h,减压浓缩除去氯化亚砜,乙醚洗涤产物,得到酰氯化二乙二醇单烯丙基醚羧酸酯;Step b) adding 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride to 300ml of chloroform and stirring to dissolve, heating to 60°C, and adding 15g of pyridine dropwise at the temperature for 3h, adding chloroform and saturated sodium bicarbonate solution for extraction after the reaction, drying the organic phase and washing with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, then dissolving it in N,N-dimethylformamide, adding 200mL of thionyl chloride dropwise in a nitrogen atmosphere, heating to 60°C for reaction for 8h, concentrating under reduced pressure to remove thionyl chloride, and washing the product with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

步骤c)将100g酰氯化二乙二醇单烯丙基醚羧酸酯加入四口烧瓶中,在加入100ml的DMF溶液重复溶解之后,升温至80℃加入5.8g乙醇胺,冷凝回流12h,之后将2.2g二甲基烷基氯化铵和20ml的DMF溶液滴加1h后,冷凝回流12h,全程均在氮气氛围下进行。反应结束后,将反应产物进行抽滤和旋蒸制备封端季铵盐二乙二醇单烯丙基醚羧酸酯。Step c) 100g of diethylene glycol monoallyl ether carboxylate acyl chloride is added to a four-necked flask, and after adding 100ml of DMF solution and dissolving repeatedly, the temperature is raised to 80°C, 5.8g of ethanolamine is added, and the mixture is condensed and refluxed for 12h, and then 2.2g of dimethyl alkyl ammonium chloride and 20ml of DMF solution are added dropwise for 1h, and the mixture is condensed and refluxed for 12h, all of which are carried out under a nitrogen atmosphere. After the reaction is completed, the reaction product is filtered and rotary evaporated to prepare a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate.

(3)制备EPEG型聚羧酸减水剂: (3) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,4g氯化烯丙基磷酸二甲酯B搅匀后调节温度在10~15℃区间,备用。将20g丙烯酸、4g季铵盐聚醚酯单体和30g水配成A液;将4g甲基丙烯磺酸钠、1.2g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water to a four-necked flask, stir and dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration is 1%), 2g of KH550, and 4g of dimethyl chloroallyl phosphate B, stir well, adjust the temperature to 10-15°C, and set aside. Prepare liquid A with 20g of acrylic acid, 4g of quaternary ammonium salt polyether ester monomer, and 30g of water; prepare liquid B with 4g of sodium methyl propylene sulfonate, 1.2g of mercaptopropionic acid monomer, and 50g of water; prepare liquid C with 0.25g of bleaching powder and 50g of water. Before adding, add 2.5g of hydrogen peroxide to a four-necked flask, stir for 5 minutes, and then start to add simultaneously, wherein liquid A and liquid B are added for 50min, and liquid C is added for 60min; after the addition is completed, keep warm for 1h, and the temperature does not exceed 25°C throughout the process. After the heat preservation is completed, liquid is added to adjust the pH value of the solution to be controlled at 5.0-6.5 to obtain an EPEG type polycarboxylate water reducer.

对比例1Comparative Example 1

市售聚羧酸减水剂。具体为科之杰新材料集团厂家生产的Point-R牌号。Commercially available polycarboxylic acid water reducer. Specifically, the Point-R brand produced by KZJ New Materials Group.

对比例2Comparative Example 2

(1)制备封端季铵盐二乙二醇单烯丙基醚羧酸酯,即季铵盐聚醚酯单体:(1) Preparation of blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate, i.e., quaternary ammonium salt polyether ester monomer:

步骤a)将100g二乙二醇单烯丙基醚分子量为1200、67g L-天冬氨酸和0.85g催化剂(硫酸铜)加入反应釜中,搅拌均匀,放置于100℃下反应6h后冷却到室温,之后在将250m三氯甲烷加入反应釜中,搅拌均匀后静置12h后后过滤,滤液在60℃下减压蒸除三氯甲烷,即得二乙二醇单烯丙基醚天冬氨酸酯;Step a) 100g of diethylene glycol monoallyl ether with a molecular weight of 1200, 67g of L-aspartic acid and 0.85g of a catalyst (copper sulfate) are added to a reactor, stirred evenly, placed at 100°C for reaction for 6 hours and then cooled to room temperature, then 250ml of chloroform is added to the reactor, stirred evenly and allowed to stand for 12 hours and then filtered, and the filtrate is evaporated under reduced pressure at 60°C to remove chloroform, thereby obtaining diethylene glycol monoallyl ether aspartic acid ester;

步骤b)将100g二乙二醇单烯丙基醚羧酸酯和60g丁二酸酐加入300三氯甲烷中搅拌溶解后,升温至60℃,并且在该温度下滴加15g吡啶,滴加时间为3h,反应后加入三氯甲烷和饱和碳酸氢钠溶液萃取,将有机相干燥后用乙醚洗涤,得到端羧基二乙二醇单烯丙基醚羧酸酯,然后溶解到N,N-二甲基甲酰胺中,在氮气氛围中滴加200mL的氯化亚砜,升温至60℃反应8h,减压浓缩除去氯化亚砜,乙醚洗涤产物,得到酰氯化二乙二醇单烯丙基醚羧酸酯;Step b) adding 100g of diethylene glycol monoallyl ether carboxylate and 60g of succinic anhydride to 300ml of chloroform and stirring to dissolve, heating to 60°C, and adding 15g of pyridine dropwise at the same temperature for 3h, adding chloroform and saturated sodium bicarbonate solution for extraction after the reaction, drying the organic phase and washing with ether to obtain terminal carboxyl diethylene glycol monoallyl ether carboxylate, then dissolving it in N,N-dimethylformamide, adding 200mL of thionyl chloride dropwise in a nitrogen atmosphere, heating to 60°C for reaction for 8h, concentrating under reduced pressure to remove thionyl chloride, and washing the product with ether to obtain acyl chloride diethylene glycol monoallyl ether carboxylate;

步骤c)将100g酰氯化二乙二醇单烯丙基醚羧酸酯加入四口烧瓶中,在加入100ml的DMF溶液重复溶解之后,升温至80℃加入5.8g乙醇胺,冷凝回流12h,之后将2.2g 二甲基烷基氯化铵和20ml的DMF溶液滴加1h后,冷凝回流12h,全程均在氮气氛围下进行。反应结束后,将反应产物进行抽滤和旋蒸制备封端季铵盐二乙二醇单烯丙基醚羧酸酯。Step c) 100 g of diethylene glycol monoallyl ether carboxylate was added to a four-necked flask, and after repeated dissolution with 100 ml of DMF solution, the temperature was raised to 80° C., 5.8 g of ethanolamine was added, and the mixture was condensed and refluxed for 12 h, and then 2.2 g of After dimethyl alkyl ammonium chloride and 20 ml of DMF solution were added dropwise for 1 hour, the mixture was condensed and refluxed for 12 hours, all under a nitrogen atmosphere. After the reaction was completed, the reaction product was filtered and rotary evaporated to prepare a blocked quaternary ammonium salt of diethylene glycol monoallyl ether carboxylate.

(2)制备EPEG型聚羧酸减水剂:(2) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,1g次磷酸钠,搅匀后调节温度在10~15℃区间,备用。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water into a four-necked flask, stir to dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration is 1%), 2g of KH550, and 1g of sodium hypophosphite, stir well and adjust the temperature to 10-15°C for use.

将20g丙烯酸、4g季铵盐聚醚酯单体和30g水配成A液;将4g AMPS、0.8g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。20g acrylic acid, 4g quaternary ammonium salt polyether ester monomer and 30g water are prepared into liquid A; 4g AMPS, 0.8g mercaptopropionic acid monomer and 50g water are prepared into liquid B; 0.25g bleaching powder and 50g water are prepared into liquid C. Before adding, add 2.5g hydrogen peroxide into a four-necked flask and stir for 5 minutes before adding simultaneously, wherein liquid A and liquid B are added for 50min, and liquid C is added for 60min; after the addition is completed, keep warm for 1h, and the temperature does not exceed 25℃ throughout the process. After the insulation is completed, add liquid to adjust the pH value of the solution to 5.0-6.5, and obtain EPEG type polycarboxylic acid water reducer.

对比例3Comparative Example 3

(1)制备氯化烯丙基磷酸二甲酯B:(1) Preparation of allyl dimethyl phosphate B:

将100g烯丙基磷酸二甲酯、300g二氯甲烷和50g乙腈溶剂投入四口烧瓶装置中,搅拌均匀后,加入催化剂4gDMF和1.5g吡啶和阻聚剂0.3g吩噻嗪和0.25g氯化亚铁。然后在搅拌过程中升温至45℃,并在该温度下滴加125g氯化亚砜,滴加时间约为3h,并在冷凝回流中保温4h,全程均在氮气气氛中反应。应结束后过滤、旋蒸处理后制备可得氯化烯丙基磷酸二甲酯B。100g of allyl dimethyl phosphate, 300g of dichloromethane and 50g of acetonitrile solvent were put into a four-necked flask device, stirred evenly, and then 4g of DMF, 1.5g of pyridine, 0.3g of phenothiazine and 0.25g of ferrous chloride were added as catalysts. Then, the temperature was raised to 45°C during stirring, and 125g of thionyl chloride was added dropwise at this temperature for about 3h, and the temperature was kept for 4h in condensation reflux, and the whole process was reacted in a nitrogen atmosphere. After the reaction was completed, filtration and rotary evaporation were performed to obtain allyl dimethyl phosphate B.

(2)制备EPEG型聚羧酸减水剂:(2) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,1g次磷酸钠,4g氯化烯丙基磷酸二甲酯B搅匀后调节温度在10~15℃区间,备用。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water into a four-necked flask, stir to dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration is 1%), 2g of KH550, 1g of sodium hypophosphite, and 4g of dimethyl chloroallyl phosphate B, stir well, adjust the temperature to 10-15°C, and set aside.

将20g丙烯酸和30g水配成A液;将4g AMPS、0.8g巯基丙酸单体和50g水配置成B 液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。20g acrylic acid and 30g water were mixed into liquid A; 4g AMPS, 0.8g mercaptopropionic acid monomer and 50g water were mixed into liquid B Liquid; 0.25g of bleaching powder and 50g of water are prepared into liquid C. Before adding, 2.5g of hydrogen peroxide is added to a four-necked flask and stirred for 5 minutes before adding simultaneously, wherein liquids A and B are added for 50min, and liquid C is added for 60min; after the addition is completed, the temperature is kept for 1h, and the temperature does not exceed 25°C throughout the process. After the insulation is completed, liquid is added to adjust the pH value of the solution to 5.0-6.5, and an EPEG type polycarboxylate water reducer is obtained.

对比例4Comparative Example 4

(1)制备EPEG型聚羧酸减水剂:(1) Preparation of EPEG type polycarboxylate water reducer:

将200g乙二醇单乙烯基聚乙二醇醚和200g去离子水加入四口烧瓶中,搅拌溶解后,之后加入4g丙烯酰胺、1g硫酸亚铁(浓度为1%)、2gKH550,1g次磷酸钠,搅匀后调节温度在10~15℃区间,备用。Add 200g of ethylene glycol monovinyl polyglycol ether and 200g of deionized water into a four-necked flask, stir to dissolve, then add 4g of acrylamide, 1g of ferrous sulfate (concentration is 1%), 2g of KH550, and 1g of sodium hypophosphite, stir well and adjust the temperature to 10-15°C for use.

将20g丙烯酸和30g水配成A液;将4g AMPS、0.8g巯基丙酸单体和50g水配置成B液;将0.25g吊白块和50g水配成C液。在滴加之前将2.5g的过氧化氢加入四口烧瓶中后搅拌5分钟后开始同时滴加,其中A、B液体滴加50min,C液滴加60min;滴加完成后保温1h,全程温度不超过25℃。保温结束后加入液体调整溶液pH值控制在5.0~6.5,得到EPEG型聚羧酸减水剂。20g acrylic acid and 30g water were prepared into liquid A; 4g AMPS, 0.8g mercaptopropionic acid monomer and 50g water were prepared into liquid B; 0.25g bleaching powder and 50g water were prepared into liquid C. Before adding, 2.5g hydrogen peroxide was added to a four-necked flask and stirred for 5 minutes before adding simultaneously, with liquids A and B added for 50min and liquid C added for 60min; after adding, the temperature was kept warm for 1h, and the temperature did not exceed 25℃. After the insulation, liquid was added to adjust the pH value of the solution to 5.0-6.5, and an EPEG type polycarboxylic acid water reducer was obtained.

采用润丰水泥(P·O 42.5)、机制砂、碎石为原料,混凝土配合比为:水泥360kg/m3、粉煤灰(II级)80kg/m3、矿粉60kg/m3、砂750kg/m3、石子980kg/m3,扩展度控制在650±20mm,分别将实施例和对比例的聚羧酸减水剂样品,根据GB8076-2008《混凝土外加剂》、GB 8077—2012《混凝土外加剂匀质性试验方法》及GJ281-2012《高强混凝土应用技术规程》,进行其混凝土初始坍落度和扩展度、经时坍落度和扩展度、倒坍落度桶排空时间、经时倒坍落度桶排空时间的测试,所得测试结果如表1所示:Runfeng cement (PO 42.5), machine-made sand and crushed stone were used as raw materials. The concrete mix ratio was: cement 360kg/m 3 , fly ash (grade II) 80kg/m 3 , mineral powder 60kg/m 3 , sand 750kg/m 3 , gravel 980kg/m 3 , and the expansion was controlled at 650±20mm. The polycarboxylate water-reducing agent samples of the embodiment and the comparative example were respectively tested for initial slump and expansion of the concrete, slump and expansion over time, emptying time of the inverted slump bucket, and emptying time of the inverted slump bucket over time according to GB8076-2008 "Concrete Admixtures", GB 8077-2012 "Test Method for Homogeneity of Concrete Admixtures" and GJ281-2012 "Technical Specification for Application of High-Strength Concrete". The test results are shown in Table 1:

表1性能对比

Table 1 Performance comparison

从表1可以看出:From Table 1 we can see that:

实施例1-5和对比例1-4的实验结果说明:在混凝土实验中,控制初始的扩展度在一定范围的情况下,本发明实施例制备得聚羧酸减水剂在掺杂使用过程中,其掺量远低于基准样(对比例1),且实施例的排空时间明显低于对比例,可以说明本发明实施例的混凝土的应用性能(排空时间)远比基准样和对比例好。The experimental results of Examples 1-5 and Comparative Examples 1-4 show that in the concrete experiment, when the initial expansion degree is controlled within a certain range, the polycarboxylate water-reducing agent prepared by the embodiment of the present invention has a much lower dosage than the reference sample (Comparative Example 1) during the doping process, and the emptying time of the embodiment is significantly lower than that of the comparative example, which can indicate that the application performance (emptying time) of the concrete of the embodiment of the present invention is much better than that of the reference sample and the comparative example.

对比例2与实施例4的区别仅在于:共聚反应中没有加入氯化烯丙基磷酸二甲酯,相比实施例4,对比例2的排空时间明显增大,表明对比例2中的混凝土粘度大,这是由于本发明方案中引入的磷酸根对水泥具有强的吸附能力,有利于其对水泥的润湿、吸附,提高混凝土的分散性和流动性,降低混凝土粘度。The only difference between Comparative Example 2 and Example 4 is that no dimethyl chloroallyl phosphate is added in the copolymerization reaction. Compared with Example 4, the emptying time of Comparative Example 2 is significantly increased, indicating that the viscosity of the concrete in Comparative Example 2 is large. This is because the phosphate introduced in the scheme of the present invention has a strong adsorption capacity for cement, which is beneficial to its wetting and adsorption of cement, improves the dispersibility and fluidity of concrete, and reduces the viscosity of concrete.

对比例3与实施例4的区别仅在于:共聚反应中没有加入季铵盐聚醚酯单体,相比实施例4,对比例3的排空时间明显增大,表明对比例3的混凝土粘度大,这是由于本发明方案中引入的季铵盐基团能够静电吸附于水泥颗粒表面,进而展现出良好的分散性以及流动性,有效降低混凝土粘度。The only difference between Comparative Example 3 and Example 4 is that no quaternary ammonium salt polyether ester monomer is added in the copolymerization reaction. Compared with Example 4, the emptying time of Comparative Example 3 is significantly increased, indicating that the concrete viscosity of Comparative Example 3 is large. This is because the quaternary ammonium salt group introduced in the scheme of the present invention can be electrostatically adsorbed on the surface of cement particles, thereby showing good dispersibility and fluidity, and effectively reducing the viscosity of the concrete.

对比例4与实施例4的区别仅在于:共聚反应中没有加入氯化烯丙基磷酸二甲酯和季铵盐聚醚酯单体,相比实施例4,对比例4的排空时间明显增大,表明对比例4的混凝土 粘度大,说明本发明方案中引入的磷酸根跟季铵盐基团,能够通过静电吸附以及空间位阻作用有效的对吸附于水泥颗粒表面,表明具有较好的流动性和分散性。The only difference between Comparative Example 4 and Example 4 is that no dimethyl chlorinated allyl phosphate and quaternary ammonium salt polyether ester monomer are added in the copolymerization reaction. Compared with Example 4, the emptying time of Comparative Example 4 is significantly increased, indicating that the concrete of Comparative Example 4 The high viscosity indicates that the phosphate and quaternary ammonium salt groups introduced in the solution of the present invention can be effectively adsorbed on the surface of cement particles through electrostatic adsorption and steric hindrance, indicating that it has good fluidity and dispersibility.

本发明实施例1-5提供的EPEG型聚羧酸减水剂,其排空时间短,其能够有效降低混凝土粘度,并且混凝土粘度降低,能够改善混凝土流速,则其施工性能变好,混凝土和易性提高;在达到相同扩展度的条件下,实施例中的掺量及排空时间均低于对比例;同时,本发明实施例1-5中混凝土的力学性能保持良好;综上所述,本发明实施例制备的EPEG型聚羧酸减水剂具有较好的降粘性能,能够改善混凝土的和易性及流速,同时其对混凝土的力学性能有明显提升,且无其他不良影响;该EPEG型聚羧酸减水剂具有适用性广,制备过程简便快捷且效率高等优点。The EPEG type polycarboxylate water-reducing agent provided in Examples 1-5 of the present invention has a short emptying time, which can effectively reduce the viscosity of concrete, and the reduced viscosity of concrete can improve the flow rate of concrete, so its construction performance becomes better and the workability of concrete is improved; under the condition of achieving the same expansion degree, the dosage and emptying time in the embodiment are lower than those in the comparative example; at the same time, the mechanical properties of the concrete in Examples 1-5 of the present invention remain good; in summary, the EPEG type polycarboxylate water-reducing agent prepared in the embodiment of the present invention has good viscosity reduction performance, can improve the workability and flow rate of concrete, and at the same time, it has a significant improvement on the mechanical properties of concrete without other adverse effects; the EPEG type polycarboxylate water-reducing agent has the advantages of wide applicability, simple and fast preparation process and high efficiency.

本发明提供的EPEG型聚羧酸减水剂及其制备方法,至少包括以下设计构思、作用机理和有益效果:The EPEG type polycarboxylate water reducer and its preparation method provided by the present invention at least include the following design concepts, action mechanisms and beneficial effects:

1.本发明根据聚羧酸减水剂结构可设计的角度,通过分子设计研制得到上述EPEG型聚羧酸减水剂,该EPEG型聚羧酸减水剂通过乙二醇单乙烯基聚乙二醇醚(EPEG)、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯及季铵盐聚醚酯单体共聚而成,在聚合物分子结构中引入磷酸根、羧酸根、酰胺基、磺酸基、季铵盐基团、硅烷基团。1. The present invention is based on the designable structure of the polycarboxylate water-reducing agent, and the EPEG type polycarboxylate water-reducing agent is developed by molecular design. The EPEG type polycarboxylate water-reducing agent is prepared by copolymerizing ethylene glycol monovinyl polyethylene glycol ether (EPEG), unsaturated amide monomers, unsaturated carboxylic acid monomers, unsaturated sulfonates, silane monomers, dimethyl chloroallyl phosphate and quaternary ammonium salt polyether ester monomers, and phosphate, carboxylate, amide, sulfonic acid, quaternary ammonium salt and silane groups are introduced into the polymer molecular structure.

其中,磷酸根对水泥具有强的吸附能力,与羧酸根协同作用,有利于其对水泥的润湿、吸附,提高混凝土的分散性和流动性;酰胺基在一定程度上使羧基得到了保护,降低了减水剂中羧基对水泥颗粒的初期吸附速率,在碱性环境下会逐步水解,再释放出羧基,羧基会持续缓慢地对水泥颗粒进行吸附,从而表现出良好的分散性和流动性。硅烷基团能将含双键的烷氧基硅烷通过自由基聚合引入PCEs的主链上,水解后可与胶凝材料化学键合,且其结合能力比静电吸附更强,因而胶凝材料颗粒与液相的固液界面能较低,胶凝材料颗粒表面的结合水少、水膜厚度小,体系中有更多的自由水,从而展现出良好的分散性和流动性。季铵盐基团能够静电吸附于水泥颗粒表面,进而展现出良好的分散性。 Among them, phosphate has a strong adsorption capacity for cement, and works synergistically with carboxylate, which is beneficial to its wetting and adsorption of cement, and improves the dispersibility and fluidity of concrete; amide group protects carboxyl group to a certain extent, reduces the initial adsorption rate of carboxyl group in water reducer to cement particles, and gradually hydrolyzes in alkaline environment, and then releases carboxyl group, which will continue to slowly adsorb cement particles, thus showing good dispersibility and fluidity. Silane group can introduce double-bonded alkoxysilane into the main chain of PCEs through free radical polymerization, and can chemically bond with cementitious materials after hydrolysis, and its binding ability is stronger than electrostatic adsorption, so the solid-liquid interface energy between cementitious material particles and liquid phase is low, the bound water on the surface of cementitious material particles is less, the water film thickness is small, and there is more free water in the system, thus showing good dispersibility and fluidity. Quaternary ammonium salt group can be electrostatically adsorbed on the surface of cement particles, thereby showing good dispersibility.

通过上述磷酸根、羧酸根、酰胺基、磺酸基、季铵盐基团、硅烷基团配合,以使该EPEG型聚羧酸减水剂具有掺量低、和易性好、能够显著降低浆体粘度等优点。By combining the above-mentioned phosphate group, carboxylate group, amide group, sulfonic acid group, quaternary ammonium salt group and silane group, the EPEG type polycarboxylate water reducer has the advantages of low dosage, good workability and the ability to significantly reduce the slurry viscosity.

2.本发明提供的EPEG型聚羧酸减水剂具有掺量低、减水率高、和易性好,能够显著降低浆体粘度、砂石料含泥量适应范围广等优点。2. The EPEG type polycarboxylate water reducer provided by the present invention has the advantages of low dosage, high water reduction rate, good workability, and can significantly reduce the viscosity of the slurry and has a wide adaptability to the mud content of sand and gravel.

3.本发明提供的EPEG型聚羧酸减水剂,其制备过程所需的原料普通易得,成本低廉,且制备过程简便快捷,绿色环保。3. The EPEG type polycarboxylate water reducer provided by the present invention has common and easily available raw materials required for its preparation process, low cost, and the preparation process is simple, fast, green and environmentally friendly.

综上所述,本发明通过聚羧酸减水剂结构可设计的角度研制上述EPEG型聚羧酸减水剂,该EPEG型聚羧酸减水剂能够有效降低混凝土粘度,提升混凝土和易性;其具有高减水性、良好的混凝土性能、适应性好,工艺简单等优点。且其制备方法过程,具有所需原料来源廉价易得、对环境友好,反应条件易控制生产工艺简单,生产成本低、合成时间短、效率高、能耗低等优点。In summary, the present invention develops the above-mentioned EPEG type polycarboxylate water-reducing agent from the perspective of the designable structure of the polycarboxylate water-reducing agent, and the EPEG type polycarboxylate water-reducing agent can effectively reduce the viscosity of concrete and improve the workability of concrete; it has the advantages of high water reduction, good concrete performance, good adaptability, simple process, etc. And its preparation method process has the advantages of cheap and easy availability of the required raw materials, environmental friendliness, easy control of reaction conditions, simple production process, low production cost, short synthesis time, high efficiency, low energy consumption, etc.

需要说明的是:It should be noted:

“乙二醇单乙烯基聚乙二醇醚”简称为EPEG;“2-丙烯酰胺-2-甲基丙磺酸”简称为AMPS,其作为不饱和磺酸盐使用的同时,也能作为链转移剂使用;"Ethylene glycol monovinyl polyethylene glycol ether" is referred to as EPEG; "2-acrylamide-2-methylpropane sulfonic acid" is referred to as AMPS, which can be used as an unsaturated sulfonate and also as a chain transfer agent;

上述实施例中的具体参数或一些常用试剂或原料,为本发明构思下的具体实施例或优选实施例,而非对其限制;本领域技术人员在本发明构思及保护范围内,可以进行适应性调整。The specific parameters or some commonly used reagents or raw materials in the above embodiments are specific embodiments or preferred embodiments of the present invention, but are not intended to limit the present invention. Those skilled in the art may make adaptive adjustments within the scope of the present invention.

最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。 Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or replace some or all of the technical features therein by equivalents. However, these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the scope of the technical solutions of the embodiments of the present invention.

Claims (10)

一种EPEG型聚羧酸减水剂,其特征在于:由共聚单体聚合而成,所述共聚单体包括乙二醇单乙烯基聚乙二醇醚、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯以及季铵盐聚醚酯单体;An EPEG type polycarboxylic acid water reducer, characterized in that: it is polymerized from comonomers, wherein the comonomers include ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomers, unsaturated carboxylic acid monomers, unsaturated sulfonates, silane monomers, chloroallyl dimethyl phosphate and quaternary ammonium salt polyether ester monomers; 所述乙二醇单乙烯基聚乙二醇醚、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯以及季铵盐聚醚酯单体的重量比为(200~300):(4~8):(20~30):(4~8):(2~4):(4~6):(4~6)。The weight ratio of the ethylene glycol monovinyl polyethylene glycol ether, the unsaturated amide monomer, the unsaturated carboxylic acid monomer, the unsaturated sulfonate, the silane monomer, the dimethyl chloride allyl phosphate and the quaternary ammonium salt polyether ester monomer is (200-300): (4-8): (20-30): (4-8): (2-4): (4-6): (4-6). 根据权利要求1所述的EPEG型聚羧酸减水剂,其特征在于:由乙二醇单乙烯基聚乙二醇醚、不饱和酰胺单体、不饱和羧酸单体、不饱和磺酸盐、硅烷单体、氯化烯丙基磷酸二甲酯以及季铵盐聚醚酯单体于10℃~15℃下进行共聚反应制得。The EPEG type polycarboxylic acid water reducer according to claim 1 is characterized in that it is prepared by copolymerizing ethylene glycol monovinyl polyethylene glycol ether, unsaturated amide monomer, unsaturated carboxylic acid monomer, unsaturated sulfonate, silane monomer, dimethyl chloride allyl phosphate and quaternary ammonium salt polyether ester monomer at 10°C to 15°C. 根据权利要求1所述的EPEG型聚羧酸减水剂,其特征在于:所述不饱和酰胺单体为丙烯酰胺、N-(2-二甲氨基乙基)丙烯酰胺、N,N-亚甲基双丙烯酰胺、环丙酰胺、己内酰胺中的一种或多种组合;The EPEG type polycarboxylic acid water reducer according to claim 1, characterized in that: the unsaturated amide monomer is one or more combinations of acrylamide, N-(2-dimethylaminoethyl)acrylamide, N,N-methylenebisacrylamide, cyclopropaneamide, and caprolactam; 所述不饱和羧酸单体为丙烯酸、甲基丙烯酸、富马酸、马来酸酐、衣康酸中的一种或多种组合;The unsaturated carboxylic acid monomer is one or more combinations of acrylic acid, methacrylic acid, fumaric acid, maleic anhydride, and itaconic acid; 所述不饱和磺酸盐为甲基丙烯磺酸钠、苯乙烯磺酸钠、2-丙烯酰胺-2-甲基丙磺酸、十二烷基苯磺酸钠中的一种或多种组合;The unsaturated sulfonate is one or more combinations of sodium methyl propylene sulfonate, sodium styrene sulfonate, 2-acrylamide-2-methylpropane sulfonic acid, and sodium dodecylbenzene sulfonate; 所述硅烷单体为乙烯基三甲氧基硅烷、乙烯基三乙氧硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、KH550、KH570中的一种或多种组合;The silane monomer is one or more combinations of vinyl trimethoxy silane, vinyl triethoxy silane, γ-methacryloxypropyl trimethoxy silane, KH550, and KH570; 所述季铵盐聚醚酯单体为封端季铵盐二乙二醇单烯丙基醚羧酸酯。The quaternary ammonium salt polyether ester monomer is a blocked quaternary ammonium salt diethylene glycol monoallyl ether carboxylate. 根据权利要求1所述的EPEG型聚羧酸减水剂,其特征在于:所述氯化烯丙基磷酸二甲酯由烯丙基磷酸二甲酯与氯化亚砜进行酯化反应制得;The EPEG type polycarboxylate water reducer according to claim 1, characterized in that: the chlorinated allyl dimethyl phosphate is prepared by esterification reaction of allyl dimethyl phosphate and thionyl chloride; 所述烯丙基磷酸二甲酯与所述氯化亚砜的重量比为100:(100~150)。The weight ratio of the allyl dimethyl phosphate to the thionyl chloride is 100:(100-150). 根据权利要求4所述的EPEG型聚羧酸减水剂,其特征在于:所述氯化烯丙基磷酸二甲酯的制备方法为: The EPEG type polycarboxylate water reducer according to claim 4 is characterized in that: the preparation method of the chloroallyl dimethyl phosphate is: 将烯丙基磷酸二甲酯和溶剂A混合,并加入第一催化剂和阻聚剂,反应体系升温至40℃~60℃,并向反应体系内加入氯化亚砜,在40℃~60℃下酯化反应2~4h并保温3~5h,制得所述氯化烯丙基磷酸二甲酯;其中,所述氯化烯丙基磷酸二甲酯的制备全程在氮气气氛或惰性气氛下进行反应;Allyl dimethyl phosphate and solvent A are mixed, and a first catalyst and a polymerization inhibitor are added, the reaction system is heated to 40° C. to 60° C., and thionyl chloride is added to the reaction system, and an esterification reaction is carried out at 40° C. to 60° C. for 2 to 4 hours and the temperature is kept for 3 to 5 hours to obtain the chloroallyl dimethyl phosphate; wherein the preparation of the chloroallyl dimethyl phosphate is carried out under a nitrogen atmosphere or an inert atmosphere throughout the reaction; 所述烯丙基磷酸二甲酯、溶剂A、氯化亚砜、第一催化剂与阻聚剂的重量比为100:(350~400):(100~150):(5~10):(0.5~1.0)。The weight ratio of allyl dimethyl phosphate, solvent A, thionyl chloride, the first catalyst and the polymerization inhibitor is 100: (350-400): (100-150): (5-10): (0.5-1.0). 根据权利要求5所述的EPEG型聚羧酸减水剂,其特征在于:所述溶剂A为二氯甲烷、三氯甲烷、乙腈、甲苯中的一种或多种组合;The EPEG type polycarboxylate water reducer according to claim 5, characterized in that: the solvent A is one or more combinations of dichloromethane, chloroform, acetonitrile, and toluene; 所述第一催化剂为N’N二甲基甲酰胺、吡啶、4-二甲氨基吡啶、浓硫酸、乙基磺酸中的一种或多种组合;The first catalyst is one or more combinations of N'N dimethylformamide, pyridine, 4-dimethylaminopyridine, concentrated sulfuric acid, and ethylsulfonic acid; 所述阻聚剂为对苯二酚、对羟基苯甲醚、吩噻嗪、氯化亚铜、氯化铁中的一种或多种组合。The polymerization inhibitor is one or more combinations of hydroquinone, p-hydroxyanisole, phenothiazine, cuprous chloride and ferric chloride. 根据权利要求1所述的EPEG型聚羧酸减水剂,其特征在于:所述季铵盐聚醚酯单体的制备方法为:The EPEG type polycarboxylate water reducer according to claim 1, characterized in that: the preparation method of the quaternary ammonium salt polyether ester monomer is: 将二乙二醇单烯丙基醚、氨基酸、第二催化剂加入到反应釜内混合均匀,于60℃~120℃下反应2~8h后冷至室温,再将三氯甲烷加入到反应釜内混匀并静置12~24h后,即得二乙二醇单烯丙基醚羧酸酯;Add diethylene glycol monoallyl ether, amino acid and the second catalyst into a reaction kettle and mix them evenly, react at 60°C to 120°C for 2 to 8 hours and then cool to room temperature, then add chloroform into the reaction kettle, mix evenly and let stand for 12 to 24 hours to obtain diethylene glycol monoallyl ether carboxylate; 将所得的二乙二醇单烯丙基醚羧酸酯,加入不饱和酸酐和溶剂A内溶解,而后加入吡啶进行反应,得到端羧基二乙二醇单烯丙基醚羧酸酯;The obtained diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A to dissolve, and then pyridine is added to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate; 将所得的端羧基二乙二醇单烯丙基醚羧酸酯溶解到N’N-二甲基甲酰胺中,在氮气气氛或惰性气氛下加入氯化亚砜,将反应体系升温至40℃~60℃反应5h~12h,制得酰氯化二乙二醇单烯丙基醚羧酸酯;The obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under a nitrogen atmosphere or an inert atmosphere, and the reaction system is heated to 40°C to 60°C for 5h to 12h to obtain acyl chloride diethylene glycol monoallyl ether carboxylate; 在乙醇胺、N’N-二甲基甲酰胺中和季铵盐化合物混合物中加入所得的酰氯化二乙二醇单烯丙基醚羧酸酯,于65℃~90℃下反应为5~24h,制得季铵盐聚醚酯单体。 The obtained acyl chloride diethylene glycol monoallyl ether carboxylate is added to ethanolamine, N'N-dimethylformamide and a mixture of quaternary ammonium salt compounds, and the mixture is reacted at 65° C. to 90° C. for 5 to 24 hours to obtain a quaternary ammonium salt polyether ester monomer. 根据权利要求7所述的EPEG型聚羧酸减水剂,其特征在于:所述氨基酸为谷氨酸、天冬氨酸中的一种或多种组合;The EPEG type polycarboxylate water reducer according to claim 7, characterized in that: the amino acid is one or more combinations of glutamic acid and aspartic acid; 所述溶剂A为二氯甲烷、三氯甲烷、乙腈、甲苯中的一种或多种组合;The solvent A is one or more of dichloromethane, chloroform, acetonitrile and toluene; 所述第二催化剂为氯化亚砜、硫酸铜、钛酸四丁酯中的一种或多种组合;The second catalyst is one or more combinations of thionyl chloride, copper sulfate, and tetrabutyl titanate; 所述不饱和酸酐为马来酸酐、丁二酸酐中的一种或多种组合;The unsaturated anhydride is one or more combinations of maleic anhydride and succinic anhydride; 所述季铵盐化合物为氯化铵、甲基丙烯酰氧乙基三甲基氯化铵、二甲基烷基氯化铵、苄基三甲基氯化铵、矮壮素中的一种或多种组合。The quaternary ammonium salt compound is one or more combinations of ammonium chloride, methacryloyloxyethyl trimethyl ammonium chloride, dimethyl alkyl ammonium chloride, benzyl trimethyl ammonium chloride and chlormequat chloride. 一种如权利要求1-8任一项所述的EPEG型聚羧酸减水剂的制备方法,其特征在于,包括以下步骤:A method for preparing the EPEG type polycarboxylate water reducer according to any one of claims 1 to 8, characterized in that it comprises the following steps: 将乙二醇单乙烯基聚乙二醇醚溶解于水中;在乙二醇单乙烯基聚乙二醇醚水溶液中加入不饱和酰胺单体、硫酸盐、硅烷单体、氯化烯丙基磷酸二甲酯和氧化剂制得底液,并控制反应体系温度为10℃~15℃;Dissolving ethylene glycol monovinyl polyethylene glycol ether in water; adding unsaturated amide monomer, sulfate, silane monomer, dimethyl chloroallyl phosphate and oxidant to the aqueous solution of ethylene glycol monovinyl polyethylene glycol ether to prepare a base solution, and controlling the temperature of the reaction system to be 10° C. to 15° C.; 在底液中加入不饱和羧酸单体、季铵盐聚醚酯单体、不饱和磺酸盐、链转移剂以及还原剂,在10℃~15℃下进行共聚反应,制得所述EPEG型聚羧酸减水剂。Unsaturated carboxylic acid monomer, quaternary ammonium salt polyether ester monomer, unsaturated sulfonate, chain transfer agent and reducing agent are added to the base liquid, and copolymerization reaction is carried out at 10° C. to 15° C. to prepare the EPEG type polycarboxylate water reducer. 一种季铵盐聚醚酯单体,其特征在于,其制备方法如下:A quaternary ammonium salt polyether ester monomer, characterized in that its preparation method is as follows: 将二乙二醇单烯丙基醚、氨基酸、第二催化剂加入到反应釜内混合均匀,于60℃~120℃下反应2~8h后冷至室温,再将三氯甲烷加入到反应釜内混匀并静置12~24h后,即得二乙二醇单烯丙基醚羧酸酯;Add diethylene glycol monoallyl ether, amino acid and the second catalyst into a reaction kettle and mix them evenly, react at 60°C to 120°C for 2 to 8 hours and then cool to room temperature, then add chloroform into the reaction kettle, mix evenly and let stand for 12 to 24 hours to obtain diethylene glycol monoallyl ether carboxylate; 将所得的二乙二醇单烯丙基醚羧酸酯,加入不饱和酸酐和溶剂A内溶解,而后加入吡啶进行反应,得到端羧基二乙二醇单烯丙基醚羧酸酯;The obtained diethylene glycol monoallyl ether carboxylate is added into unsaturated acid anhydride and solvent A to dissolve, and then pyridine is added to react to obtain carboxyl-terminated diethylene glycol monoallyl ether carboxylate; 将所得的端羧基二乙二醇单烯丙基醚羧酸酯溶解到N’N-二甲基甲酰胺中,在氮气气氛或惰性气氛下加入氯化亚砜,将反应体系升温至40℃~60℃反应5h~12h,制得酰氯化二乙二醇单烯丙基醚羧酸酯;The obtained terminal carboxyl diethylene glycol monoallyl ether carboxylate is dissolved in N'N-dimethylformamide, thionyl chloride is added under a nitrogen atmosphere or an inert atmosphere, and the reaction system is heated to 40°C to 60°C for 5h to 12h to obtain acyl chloride diethylene glycol monoallyl ether carboxylate; 在乙醇胺、N’N-二甲基甲酰胺中和季铵盐化合物混合物中加入所得的酰氯化二乙二 醇单烯丙基醚羧酸酯,于65℃~90℃下反应为5~24h,制得季铵盐聚醚酯单体。 Add the obtained diethylene glycol chloride to the mixture of ethanolamine, N'N-dimethylformamide and quaternary ammonium salt compound. Alcohol monoallyl ether carboxylate is reacted at 65°C to 90°C for 5 to 24 hours to obtain a quaternary ammonium salt polyether ester monomer.
PCT/CN2023/138385 2022-12-16 2023-12-13 Quaternary ammonium salt polyether ester monomer, epeg type polycarboxylate water reducing agent, and preparation method therefor Ceased WO2024125545A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202211621645.8 2022-12-16
CN202211621645.8A CN116041630B (en) 2022-12-16 2022-12-16 Quaternary ammonium salt polyether ester monomer, EPEG type polycarboxylate superplasticizer and preparation method thereof

Publications (1)

Publication Number Publication Date
WO2024125545A1 true WO2024125545A1 (en) 2024-06-20

Family

ID=86130596

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2023/138385 Ceased WO2024125545A1 (en) 2022-12-16 2023-12-13 Quaternary ammonium salt polyether ester monomer, epeg type polycarboxylate water reducing agent, and preparation method therefor

Country Status (2)

Country Link
CN (1) CN116041630B (en)
WO (1) WO2024125545A1 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118638277A (en) * 2024-08-13 2024-09-13 西南石油大学 A hydrophobic long-chain antiscalant and its preparation method and application
CN118834050A (en) * 2024-07-16 2024-10-25 广东泷江源水泥制品有限公司 Self-compaction high performance concrete cable apron
CN118894695A (en) * 2024-10-08 2024-11-05 中建材(合肥)粉体科技装备有限公司 A modified mineral admixture concrete and preparation method thereof
CN119118552A (en) * 2024-09-09 2024-12-13 中交四航局第一工程有限公司 A core material for concrete and its application in ultra-high performance concrete
CN119219359A (en) * 2024-08-29 2024-12-31 江西铜业技术研究院有限公司 Ultrafine full tailings filling paste water reducing agent and its preparation method and application
CN119285297A (en) * 2024-10-09 2025-01-10 重庆市鲁渝矿业发展有限公司 Cement material containing barium slag and preparation method thereof
CN119859227A (en) * 2025-02-15 2025-04-22 江苏东宝农化股份有限公司 Preparation method of polycarboxylate dispersant and application of polycarboxylate dispersant in pesticides
CN120192093A (en) * 2025-05-22 2025-06-24 广东兴辉陶瓷集团有限公司 A protective glaze for rock plate surface and preparation method thereof
CN120248238A (en) * 2025-05-29 2025-07-04 安徽森普新型材料发展有限公司 A high-slump-retention polycarboxylate water-reducing agent and its preparation method and use

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116041630B (en) * 2022-12-16 2024-07-26 科之杰新材料集团有限公司 Quaternary ammonium salt polyether ester monomer, EPEG type polycarboxylate superplasticizer and preparation method thereof
CN116655865B (en) * 2023-08-01 2023-09-22 邢台建工商品混凝土有限公司 Preparation process and application of modified polycarboxylic acid type high-efficiency water reducer
CN117776618B (en) * 2023-12-11 2025-02-14 上海宏韵新型建材有限公司 Concrete containing polycarboxylate water reducer and preparation process thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120016059A1 (en) * 2009-03-25 2012-01-19 Lafarge Gypsum International Water-reducing agent for hydraulic binders
JP2015127270A (en) * 2013-12-27 2015-07-09 株式会社日本触媒 Cement additive
CN109824836A (en) * 2019-01-29 2019-05-31 广东瑞安科技实业有限公司 Workability is good, wide adaptability polycarboxylate water-reducer and preparation method thereof
CN109880019A (en) * 2019-01-29 2019-06-14 广东瑞安科技实业有限公司 A kind of workability is good, wide adaptability polycarboxylate water-reducer and preparation method thereof
CN109970927A (en) * 2019-04-23 2019-07-05 四川同舟化工科技有限公司 A kind of high-thin arch dam ultra early-strength polycarboxylate water-reducer and preparation method thereof
CN112979887A (en) * 2021-03-01 2021-06-18 佛山市凯隽新建材科技有限公司 Modified polycarboxylic acid, preparation method thereof and application of modified polycarboxylic acid as water reducing agent
CN113754842A (en) * 2021-10-21 2021-12-07 上海三瑞高分子材料股份有限公司 Amphoteric anti-mud polycarboxylate superplasticizer
CN116041630A (en) * 2022-12-16 2023-05-02 科之杰新材料集团有限公司 Quaternary ammonium salt polyether ester monomer, EPEG type polycarboxylate superplasticizer and preparation method thereof

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015189680A (en) * 2014-03-27 2015-11-02 Kjケミカルズ株式会社 unsaturated quaternary ammonium salt
CN107383285A (en) * 2017-08-16 2017-11-24 科之杰新材料集团有限公司 A kind of preparation method of ethers polycarboxylic acid water reducing agent
CN111484582A (en) * 2020-04-02 2020-08-04 厦门路桥翔通建材科技有限公司 Viscosity-reducing polycarboxylate superplasticizer and preparation method thereof
CN114213601A (en) * 2021-12-27 2022-03-22 中建西部建设新材料科技有限公司 Hydrolysis regulation slow-release anti-mud polycarboxylate superplasticizer and preparation method thereof

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120016059A1 (en) * 2009-03-25 2012-01-19 Lafarge Gypsum International Water-reducing agent for hydraulic binders
JP2015127270A (en) * 2013-12-27 2015-07-09 株式会社日本触媒 Cement additive
CN109824836A (en) * 2019-01-29 2019-05-31 广东瑞安科技实业有限公司 Workability is good, wide adaptability polycarboxylate water-reducer and preparation method thereof
CN109880019A (en) * 2019-01-29 2019-06-14 广东瑞安科技实业有限公司 A kind of workability is good, wide adaptability polycarboxylate water-reducer and preparation method thereof
CN109970927A (en) * 2019-04-23 2019-07-05 四川同舟化工科技有限公司 A kind of high-thin arch dam ultra early-strength polycarboxylate water-reducer and preparation method thereof
CN112979887A (en) * 2021-03-01 2021-06-18 佛山市凯隽新建材科技有限公司 Modified polycarboxylic acid, preparation method thereof and application of modified polycarboxylic acid as water reducing agent
CN113754842A (en) * 2021-10-21 2021-12-07 上海三瑞高分子材料股份有限公司 Amphoteric anti-mud polycarboxylate superplasticizer
CN116041630A (en) * 2022-12-16 2023-05-02 科之杰新材料集团有限公司 Quaternary ammonium salt polyether ester monomer, EPEG type polycarboxylate superplasticizer and preparation method thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118834050A (en) * 2024-07-16 2024-10-25 广东泷江源水泥制品有限公司 Self-compaction high performance concrete cable apron
CN118638277A (en) * 2024-08-13 2024-09-13 西南石油大学 A hydrophobic long-chain antiscalant and its preparation method and application
CN119219359A (en) * 2024-08-29 2024-12-31 江西铜业技术研究院有限公司 Ultrafine full tailings filling paste water reducing agent and its preparation method and application
CN119118552A (en) * 2024-09-09 2024-12-13 中交四航局第一工程有限公司 A core material for concrete and its application in ultra-high performance concrete
CN119118552B (en) * 2024-09-09 2025-03-07 中交四航局第一工程有限公司 Core material for concrete and application of core material in ultra-high performance concrete
CN118894695A (en) * 2024-10-08 2024-11-05 中建材(合肥)粉体科技装备有限公司 A modified mineral admixture concrete and preparation method thereof
CN119285297A (en) * 2024-10-09 2025-01-10 重庆市鲁渝矿业发展有限公司 Cement material containing barium slag and preparation method thereof
CN119859227A (en) * 2025-02-15 2025-04-22 江苏东宝农化股份有限公司 Preparation method of polycarboxylate dispersant and application of polycarboxylate dispersant in pesticides
CN120192093A (en) * 2025-05-22 2025-06-24 广东兴辉陶瓷集团有限公司 A protective glaze for rock plate surface and preparation method thereof
CN120248238A (en) * 2025-05-29 2025-07-04 安徽森普新型材料发展有限公司 A high-slump-retention polycarboxylate water-reducing agent and its preparation method and use

Also Published As

Publication number Publication date
CN116041630A (en) 2023-05-02
CN116041630B (en) 2024-07-26

Similar Documents

Publication Publication Date Title
WO2024125545A1 (en) Quaternary ammonium salt polyether ester monomer, epeg type polycarboxylate water reducing agent, and preparation method therefor
CN114195421B (en) Preparation method of polycarboxylic acid additive for machine-made sand concrete
CN103613306B (en) A kind of poly carboxylic acid series water reducer containing hyperbranched polyamine-ester structure and preparation method thereof
CN113372549B (en) Vinyl-terminated hyperbranched polymer, viscosity-reducing polycarboxylate superplasticizer with hyperbranched structure and preparation method of viscosity-reducing polycarboxylate superplasticizer
CN106832147B (en) A kind of preparation method of the polycarboxylate water-reducer containing phosphonyl group
CN101851323B (en) Multi-branched polycarboxylic acid water reducing agent with excellent slump retaining performance and preparation method thereof
CN104140503A (en) Method for synthesizing high-water-reduction high-slump-retaining high-performance polycarboxylate water reducer at normal temperature
CN110305262A (en) A kind of amphoteric early-strength polycarboxylate superplasticizer mother liquor for C30 concrete
CN107629173B (en) Method for preparing polycarboxylate slump retention agent by atom transfer radical polymerization
CN112159500B (en) Anti-mud polycarboxylic acid high-performance water reducing agent and preparation method and application thereof
CN106117468A (en) The preparation method of the height anti-chamotte mould cement water reducing agent of graft copolymerization cationic side chain
CN115838458A (en) A kind of novel polycarboxylate superplasticizer and preparation method thereof
CN115975124A (en) Hyperbranched polyether monomer, hyperbranched EPEG type polycarboxylate superplasticizer and preparation method thereof
CN116284737A (en) Hyperbranched polyether and preparation method thereof
CN107446088A (en) A kind of preparation method of the high water reducing type polycarboxylate water-reducer of high solids content ethers
CN115612086B (en) Double-arm side chain structure monomer and preparation method thereof, and water reducing agent and preparation method thereof
CN115594804A (en) A kind of preparation method of anti-flocculation type amphoteric polycarboxylate water reducer
CN114195956A (en) High-strength concrete viscosity-reducing water reducer and preparation method thereof
CN109535346B (en) Anti-clay polycarboxylate superplasticizer and preparation method and application thereof
CN112126021B (en) A kind of anti-mud type polycarboxylate water reducer and preparation method thereof
CN113683735B (en) Concrete additive and preparation method and application thereof
CN113912833B (en) Esterified monomer, esterified product, high-adaptability polycarboxylic acid slump retaining agent and preparation method thereof
CN117430399A (en) Full solid waste clinker-free controllable low-strength material and preparation method thereof
CN117777474A (en) Sustained-release polycarboxylate water reducer modified graphene oxide, and preparation method and application thereof
CN114516938A (en) Non-chlorine double-comb type amphoteric polycarboxylate superplasticizer and preparation method thereof

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 23902741

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 23902741

Country of ref document: EP

Kind code of ref document: A1