CN114671982A - A kind of shrinkage-reducing polycarboxylate water-reducing agent and preparation method thereof - Google Patents
A kind of shrinkage-reducing polycarboxylate water-reducing agent and preparation method thereof Download PDFInfo
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- CN114671982A CN114671982A CN202210169327.6A CN202210169327A CN114671982A CN 114671982 A CN114671982 A CN 114671982A CN 202210169327 A CN202210169327 A CN 202210169327A CN 114671982 A CN114671982 A CN 114671982A
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- Prior art keywords
- shrinkage
- reducing
- aqueous solution
- reducing agent
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- 239000003638 chemical reducing agent Substances 0.000 title claims abstract description 81
- 229920005646 polycarboxylate Polymers 0.000 title claims abstract description 78
- 238000002360 preparation method Methods 0.000 title claims abstract description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 88
- 239000012153 distilled water Substances 0.000 claims abstract description 59
- 239000000178 monomer Substances 0.000 claims abstract description 54
- 239000003999 initiator Substances 0.000 claims abstract description 24
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 22
- 229920000570 polyether Polymers 0.000 claims abstract description 22
- 239000002994 raw material Substances 0.000 claims abstract description 19
- 239000002270 dispersing agent Substances 0.000 claims abstract description 11
- 239000002253 acid Substances 0.000 claims abstract description 8
- 125000000542 sulfonic acid group Chemical group 0.000 claims abstract description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 124
- 239000007864 aqueous solution Substances 0.000 claims description 89
- 238000006243 chemical reaction Methods 0.000 claims description 68
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 50
- 229920000151 polyglycol Polymers 0.000 claims description 47
- 239000010695 polyglycol Substances 0.000 claims description 47
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 claims description 42
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 42
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 claims description 42
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 41
- 239000000243 solution Substances 0.000 claims description 40
- CPJRRXSHAYUTGL-UHFFFAOYSA-N isopentenyl alcohol Chemical compound CC(=C)CCO CPJRRXSHAYUTGL-UHFFFAOYSA-N 0.000 claims description 36
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 33
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 33
- LCPVQAHEFVXVKT-UHFFFAOYSA-N 2-(2,4-difluorophenoxy)pyridin-3-amine Chemical compound NC1=CC=CN=C1OC1=CC=C(F)C=C1F LCPVQAHEFVXVKT-UHFFFAOYSA-N 0.000 claims description 32
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Substances [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 claims description 32
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 30
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 claims description 29
- 150000003839 salts Chemical class 0.000 claims description 28
- 238000003756 stirring Methods 0.000 claims description 27
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 25
- -1 alkylene glycol Chemical compound 0.000 claims description 23
- DKIDEFUBRARXTE-UHFFFAOYSA-N 3-mercaptopropanoic acid Chemical compound OC(=O)CCS DKIDEFUBRARXTE-UHFFFAOYSA-N 0.000 claims description 22
- 229920001002 functional polymer Polymers 0.000 claims description 22
- 239000002202 Polyethylene glycol Substances 0.000 claims description 20
- 229920001223 polyethylene glycol Polymers 0.000 claims description 20
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 19
- DPBJAVGHACCNRL-UHFFFAOYSA-N 2-(dimethylamino)ethyl prop-2-enoate Chemical compound CN(C)CCOC(=O)C=C DPBJAVGHACCNRL-UHFFFAOYSA-N 0.000 claims description 17
- KWIUHFFTVRNATP-UHFFFAOYSA-N Betaine Natural products C[N+](C)(C)CC([O-])=O KWIUHFFTVRNATP-UHFFFAOYSA-N 0.000 claims description 17
- KWIUHFFTVRNATP-UHFFFAOYSA-O N,N,N-trimethylglycinium Chemical compound C[N+](C)(C)CC(O)=O KWIUHFFTVRNATP-UHFFFAOYSA-O 0.000 claims description 17
- 229960003237 betaine Drugs 0.000 claims description 17
- 229910052757 nitrogen Inorganic materials 0.000 claims description 15
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 14
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 14
- 229920001577 copolymer Polymers 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 12
- CWERGRDVMFNCDR-UHFFFAOYSA-N thioglycolic acid Chemical compound OC(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-N 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 10
- 125000002947 alkylene group Chemical group 0.000 claims description 9
- NLVXSWCKKBEXTG-UHFFFAOYSA-N vinylsulfonic acid Chemical compound OS(=O)(=O)C=C NLVXSWCKKBEXTG-UHFFFAOYSA-N 0.000 claims description 9
- XEEYSDHEOQHCDA-UHFFFAOYSA-N 2-methylprop-2-ene-1-sulfonic acid Chemical compound CC(=C)CS(O)(=O)=O XEEYSDHEOQHCDA-UHFFFAOYSA-N 0.000 claims description 8
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims description 8
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 8
- MRUAUOIMASANKQ-UHFFFAOYSA-O carboxymethyl-[3-(dodecanoylamino)propyl]-dimethylazanium Chemical compound CCCCCCCCCCCC(=O)NCCC[N+](C)(C)CC(O)=O MRUAUOIMASANKQ-UHFFFAOYSA-O 0.000 claims description 7
- 229940075468 lauramidopropyl betaine Drugs 0.000 claims description 7
- 125000000217 alkyl group Chemical group 0.000 claims description 6
- MRUAUOIMASANKQ-UHFFFAOYSA-N cocamidopropyl betaine Chemical compound CCCCCCCCCCCC(=O)NCCC[N+](C)(C)CC([O-])=O MRUAUOIMASANKQ-UHFFFAOYSA-N 0.000 claims description 6
- 229940073507 cocamidopropyl betaine Drugs 0.000 claims description 6
- 125000005702 oxyalkylene group Chemical group 0.000 claims description 6
- 238000006116 polymerization reaction Methods 0.000 claims description 6
- UFQHFMGRRVQFNA-UHFFFAOYSA-N 3-(dimethylamino)propyl prop-2-enoate Chemical compound CN(C)CCCOC(=O)C=C UFQHFMGRRVQFNA-UHFFFAOYSA-N 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- 229910052708 sodium Inorganic materials 0.000 claims description 4
- 239000011734 sodium Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- AUZRCMMVHXRSGT-UHFFFAOYSA-N 2-methylpropane-1-sulfonic acid;prop-2-enamide Chemical compound NC(=O)C=C.CC(C)CS(O)(=O)=O AUZRCMMVHXRSGT-UHFFFAOYSA-N 0.000 claims description 3
- 150000007513 acids Chemical class 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- WVYSWPBECUHBMJ-UHFFFAOYSA-N 2-methylprop-1-en-1-ol Chemical compound CC(C)=CO WVYSWPBECUHBMJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 2
- WNAHIZMDSQCWRP-UHFFFAOYSA-N dodecane-1-thiol Chemical compound CCCCCCCCCCCCS WNAHIZMDSQCWRP-UHFFFAOYSA-N 0.000 claims description 2
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethyl mercaptane Natural products CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 claims description 2
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 claims description 2
- ZQMHJBXHRFJKOT-UHFFFAOYSA-N methyl 2-[(1-methoxy-2-methyl-1-oxopropan-2-yl)diazenyl]-2-methylpropanoate Chemical compound COC(=O)C(C)(C)N=NC(C)(C)C(=O)OC ZQMHJBXHRFJKOT-UHFFFAOYSA-N 0.000 claims description 2
- XONPDZSGENTBNJ-UHFFFAOYSA-N molecular hydrogen;sodium Chemical compound [Na].[H][H] XONPDZSGENTBNJ-UHFFFAOYSA-N 0.000 claims description 2
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical compound OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 claims description 2
- VKEQBMCRQDSRET-UHFFFAOYSA-N Methylone Chemical compound CNC(C)C(=O)C1=CC=C2OCOC2=C1 VKEQBMCRQDSRET-UHFFFAOYSA-N 0.000 claims 1
- 150000002085 enols Chemical class 0.000 claims 1
- 125000001972 isopentyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])C([H])([H])* 0.000 claims 1
- HLERILKGMXJNBU-UHFFFAOYSA-N norvaline betaine Chemical compound CCCC(C([O-])=O)[N+](C)(C)C HLERILKGMXJNBU-UHFFFAOYSA-N 0.000 claims 1
- DOKHEARVIDLSFF-UHFFFAOYSA-N prop-1-en-1-ol Chemical compound CC=CO DOKHEARVIDLSFF-UHFFFAOYSA-N 0.000 claims 1
- 229940079827 sodium hydrogen sulfite Drugs 0.000 claims 1
- 239000004567 concrete Substances 0.000 abstract description 51
- 239000008030 superplasticizer Substances 0.000 abstract description 8
- 230000001603 reducing effect Effects 0.000 abstract description 6
- 238000005336 cracking Methods 0.000 abstract description 2
- 238000011161 development Methods 0.000 abstract description 2
- 239000003513 alkali Substances 0.000 abstract 1
- 230000001934 delay Effects 0.000 abstract 1
- 230000002401 inhibitory effect Effects 0.000 abstract 1
- ASUAYTHWZCLXAN-UHFFFAOYSA-N prenol Chemical compound CC(C)=CCO ASUAYTHWZCLXAN-UHFFFAOYSA-N 0.000 description 44
- 238000010992 reflux Methods 0.000 description 23
- 230000000694 effects Effects 0.000 description 15
- 238000002156 mixing Methods 0.000 description 12
- 239000004568 cement Substances 0.000 description 11
- 239000000203 mixture Substances 0.000 description 11
- 150000001336 alkenes Chemical class 0.000 description 10
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 10
- 230000009467 reduction Effects 0.000 description 7
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- SZHIIIPPJJXYRY-UHFFFAOYSA-M sodium;2-methylprop-2-ene-1-sulfonate Chemical compound [Na+].CC(=C)CS([O-])(=O)=O SZHIIIPPJJXYRY-UHFFFAOYSA-M 0.000 description 6
- JKNCOURZONDCGV-UHFFFAOYSA-N 2-(dimethylamino)ethyl 2-methylprop-2-enoate Chemical compound CN(C)CCOC(=O)C(C)=C JKNCOURZONDCGV-UHFFFAOYSA-N 0.000 description 5
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 5
- 125000004122 cyclic group Chemical group 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000036571 hydration Effects 0.000 description 3
- 238000006703 hydration reaction Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- 239000004480 active ingredient Substances 0.000 description 2
- 230000001476 alcoholic effect Effects 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 125000001844 prenyl group Chemical group [H]C([*])([H])C([H])=C(C([H])([H])[H])C([H])([H])[H] 0.000 description 2
- 150000003254 radicals Chemical class 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- XEUCQOBUZPQUMQ-UHFFFAOYSA-N Glycolone Chemical compound COC1=C(CC=C(C)C)C(=O)NC2=C1C=CC=C2OC XEUCQOBUZPQUMQ-UHFFFAOYSA-N 0.000 description 1
- UWIULCYKVGIOPW-UHFFFAOYSA-N Glycolone Natural products CCOC1=C(CC=CC)C(=O)N(C)c2c(O)cccc12 UWIULCYKVGIOPW-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 239000011083 cement mortar Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- HOSXICNCYBUYAW-UHFFFAOYSA-N dimethylamino prop-2-enoate Chemical compound CN(C)OC(=O)C=C HOSXICNCYBUYAW-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 125000004494 ethyl ester group Chemical group 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000013100 final test Methods 0.000 description 1
- 239000004574 high-performance concrete Substances 0.000 description 1
- 239000011372 high-strength concrete Substances 0.000 description 1
- 229940079826 hydrogen sulfite Drugs 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- LHTVMBMETNGEAN-UHFFFAOYSA-N pent-1-en-1-ol Chemical compound CCCC=CO LHTVMBMETNGEAN-UHFFFAOYSA-N 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F283/00—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
- C08F283/06—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
- C08F283/065—Macromolecular 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
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B24/00—Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
- C04B24/24—Macromolecular compounds
- C04B24/26—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C04B24/2688—Copolymers containing at least three different monomers
- C04B24/2694—Copolymers containing at least three different monomers containing polyether side chains
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F267/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated polycarboxylic acids or derivatives thereof as defined in group C08F22/00
- C08F267/04—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated polycarboxylic acids or derivatives thereof as defined in group C08F22/00 on to polymers of anhydrides
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2103/00—Function or property of ingredients for mortars, concrete or artificial stone
- C04B2103/30—Water reducers, plasticisers, air-entrainers, flow improvers
- C04B2103/302—Water reducers
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
技术领域technical field
本发明属于混凝土外加剂技术领域,尤其是涉及一种减缩型聚羧酸减水剂及其制备方法。The invention belongs to the technical field of concrete admixtures, in particular to a shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof.
背景技术Background technique
近年来,随着建筑工业的快速进步和设计水平的逐渐提升,现代混凝土也朝着高强度、高性能方向发展。然而,由于混凝土硬化成形过程中内部结构的种种原因,致使混凝土在硬化过程中过大的收缩一直成为影响混凝土工程质量的一个重要因素。混凝土常常出现两方面的收缩变形,一是混凝土的干燥收缩,此现象是由毛细孔中的水蒸发而引起的硬化混凝土收缩,是混凝土内部水分向外部挥发的结果;二是混凝土的自收缩,此现象是由自干燥或混凝土内部相对湿度降低引起的收缩,是混凝土在恒温条件下,由于水泥水化作用引起的混凝土宏观体积减小的现象。这两种收缩变形是导致混凝土结构非荷载裂缝产生的关键因素,混凝土的裂缝将导致结构渗漏、钢筋锈蚀、强度降低,进而降低混凝土的耐久性,引起结构物的破坏及坍塌,从而严重影响混凝土的安全性能及使用寿命。In recent years, with the rapid progress of the construction industry and the gradual improvement of the design level, modern concrete is also developing in the direction of high strength and high performance. However, due to various reasons of the internal structure during the hardening and forming process of concrete, the excessive shrinkage of concrete during the hardening process has always been an important factor affecting the quality of concrete projects. Concrete often undergoes two shrinkage deformations. One is the drying shrinkage of concrete. This phenomenon is the shrinkage of hardened concrete caused by the evaporation of water in the capillary pores, which is the result of the volatilization of water inside the concrete to the outside. The second is the self-shrinking of concrete. This phenomenon is the shrinkage caused by self-drying or the reduction of relative humidity inside the concrete, and it is the phenomenon that the macroscopic volume of concrete is reduced due to the hydration of cement under constant temperature conditions. These two kinds of shrinkage deformation are the key factors that lead to the occurrence of non-load cracks in concrete structures. Cracks in concrete will lead to structural leakage, corrosion of steel bars, and reduction of strength, thereby reducing the durability of concrete, causing damage and collapse of structures, thus seriously affecting Safety performance and service life of concrete.
混凝土出现收缩裂缝不仅影响结构美观,更严重的是危及建筑物的整体性、水密性和耐久性。特别是泵送混凝土、高强混凝土、高性能混凝土、高效减水剂和超细掺合料的应用,使得混凝土的裂缝问题越来越严重,如何减少混凝土的收缩一直是混凝土领域值得研究的课题。工程实践表明,一种具有减缩功能的聚羧酸减水剂,由于在聚羧酸减水剂分子结构的侧链上接枝了减缩基团,从而在具备高减水率、保强度的的同时具有良好的减缩效果,其能在一定程度上补偿收缩,延缓混凝土的裂缝产生的时间以及裂缝发展的宽度,为抑制混凝土自收缩和干缩收缩开裂开辟了新的途径。因此,研制出一种具有减缩功能的聚羧酸减水剂来改善混凝土材料结构的稳定性,减少裂缝的产生,进而提高混凝土材料结构的耐久性具有重要的实用意义。Shrinkage cracks in concrete not only affect the aesthetics of the structure, but also endanger the integrity, watertightness and durability of the building. Especially the application of pumped concrete, high-strength concrete, high-performance concrete, superplasticizer and superfine admixture makes the problem of concrete cracks more and more serious. How to reduce the shrinkage of concrete has always been a topic worthy of research in the field of concrete. Engineering practice shows that a polycarboxylate superplasticizer with shrinkage-reducing function has a high water-reducing rate and strength retention due to grafted shrinkage-reducing groups on the side chain of the molecular structure of the polycarboxylate superplasticizer. At the same time, it has a good shrinkage reduction effect, which can compensate the shrinkage to a certain extent, delay the time of concrete crack generation and the width of crack development, and open up a new way to inhibit the self-shrinkage and drying shrinkage cracking of concrete. Therefore, it is of great practical significance to develop a polycarboxylate water-reducing agent with shrinkage-reducing function to improve the stability of the concrete material structure, reduce the generation of cracks, and then improve the durability of the concrete material structure.
专利申请公开文件CN102112412B中报道了一种含有聚氧化烯基的聚醚多元醇烷烃化合物,专利报道了此减缩型减水剂掺入混凝土中可能确有一定的减缩效果,但是掺量较高,成本也较高,单纯的减缩剂掺量高,将会影响混凝土的流动性和强度。Patent application publication CN102112412B reported a polyether polyol alkane compound containing polyoxyalkylene group, and the patent reported that this shrinkage-reducing water-reducing agent may indeed have a certain shrinkage-reducing effect when mixed into concrete, but the dosage is relatively high, The cost is also high, and the high content of the simple shrinkage reducer will affect the fluidity and strength of the concrete.
专利申请公开文件CN104262545A中报道了一种低引气减缩型聚羧酸减水剂及其制备方法,专利是将各原料通过自由基聚合成了一种聚羧酸减水剂,该方法是在传统的聚羧酸减水剂的基础上稍作改进,可能有一定的减缩效果。但是最终产品与水泥、其他功能减水剂的相容性较较差,不能均匀分布在混凝土体系中。Patent application publication CN104262545A reports a low-entrainment condensation-reducing polycarboxylate water reducer and its preparation method. The patent is to polymerize the raw materials into a polycarboxylate water reducer by free radicals. A slight improvement on the basis of the traditional polycarboxylate water reducing agent may have a certain shrinkage reduction effect. However, the final product has poor compatibility with cement and other functional water reducers and cannot be uniformly distributed in the concrete system.
专利CN108164653A报道了一种减缩型聚羧酸减水剂及其制备方法,后期合成聚羧酸减水剂时,自由基共聚没有规避氧气在此过程中的氧化作用,原理上实施氮气保护更为合理,否则氧化过程将导致副产物增加且体系成分变得复杂化,致使每一批次生产的产品对混凝土的实际减缩以及减水效果无法保持一致,因此需要进一步优化工艺条件。Patent CN108164653A reports a shrinkage-reducing polycarboxylate water-reducing agent and its preparation method. When synthesizing the polycarboxylate water-reducing agent in the later stage, the free radical copolymerization does not avoid the oxidation of oxygen in this process. In principle, nitrogen protection is more effective. Reasonable, otherwise the oxidation process will lead to the increase of by-products and the complexity of the system components, so that the actual shrinkage and water-reduction effects of each batch of products cannot be consistent, so the process conditions need to be further optimized.
发明内容SUMMARY OF THE INVENTION
本发明旨在解决上述技术问题,提供一种减缩型聚羧酸减水剂及其制备方法。The present invention aims to solve the above-mentioned technical problems, and provides a condensation-reducing polycarboxylate water-reducing agent and a preparation method thereof.
为了达到上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种减缩型聚羧酸减水剂,包括以下结构的有效组分:A shrinkage-reducing polycarboxylate water-reducing agent, comprising the effective components of the following structure:
; ;
其中,a、b、c、d、x、y和z均为整数,且a=1~30,b=10~65,c=1~25,d=1~18,x=1~32,且x代表氧化烯基团(—R7—O—)的平均加成摩尔数,y=1~20,且y代表氧化烯基团(—R8—O—)的平均加成摩尔数,z=5~27;Among them, a, b, c, d, x, y and z are all integers, and a=1~30, b=10~65, c=1~25, d=1~18, x=1~32, And x represents the average added moles of oxyalkylene groups (—R7—O—), y=1~20, and y represents the average added moles of oxyalkylene groups (—R8—O—), z= 5~27;
R1和R2为—H或—CH3,R3为1~2个碳的烷基,R4为—H或1~2个碳的烷基,R5为—H或—CH3,R6为1~2个碳的烷基,R7为C2~C20的亚烷基,R8为C2~C4的亚烷基,R9为—H或2~3个碳的烷基,A为C1~C3的亚烷基,M为Na或K或NH4。R1 and R2 are -H or -CH3, R3 is an alkyl group of 1-2 carbons, R4 is -H or an alkyl group of 1-2 carbons, R5 is -H or -CH3, R6 is 1-2 carbons R7 is C2~C20 alkylene, R8 is C2~C4 alkylene, R9 is -H or 2~3 carbon alkyl, A is C1~C3 alkylene, M is C1~C3 alkylene Na or K or NH4.
一种减缩型聚羧酸减水剂的制备方法,包括以下步骤:A preparation method of a shrinkage-reducing polycarboxylate water-reducing agent, comprising the following steps:
步骤(1),减缩功能聚合单体的制备:Step (1), preparation of shrinkage-reducing functional polymerizable monomers:
在反应器中加入蒸馏水、莫尔盐和马来酸酐,加热到60℃~80℃;Add distilled water, molar salt and maleic anhydride into the reactor, and heat to 60℃~80℃;
在反应器中滴加70~74%丙烯酸水溶液、73~77%环氧丙烷水溶液、53~57%异戊二烯醇水溶液,外加13~17%的过硫酸钠、13~17%的亚硫酸氢钠作为引发剂参与反应;70-74% acrylic acid aqueous solution, 73-77% propylene oxide aqueous solution, 53-57% isoprenol aqueous solution, 13-17% sodium persulfate, 13-17% sulfurous acid are added dropwise to the reactor Sodium hydrogen participates in the reaction as an initiator;
待滴加完成后,将所得溶液在相同的受控温度下再熟化40~70分钟,反应结束后静置冷却,得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其结构单元如下:After the dropwise addition is completed, the obtained solution is further aged for 40 to 70 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling to obtain an alkylene glycol/alkenyl ether/maleic anhydride shrinkage-reducing functional copolymer, which is The structural units are as follows:
; ;
步骤(2),减缩型聚羧酸减水剂的制备:Step (2), the preparation of shrinkage-reducing polycarboxylate water-reducing agent:
在反应器中加入步骤(1)所得到的减缩功能聚合单体和蒸馏水,升温至35℃~45℃,搅拌10~30分钟;Add the shrinkage-reducing functional polymerized monomer obtained in step (1) and distilled water into the reactor, heat up to 35°C to 45°C, and stir for 10 to 30 minutes;
待减缩功能聚合单体和蒸馏水混合均匀后加入不饱和羧酸烷基酯和磺酸基单体,在氮气保护下,恒温水浴加热并搅拌;After the shrinkage-reducing functional polymer monomer and distilled water are evenly mixed, add unsaturated carboxylic acid alkyl ester and sulfonic acid group monomer, and under nitrogen protection, heat and stir in a constant temperature water bath;
当反应温度达到60℃~75℃时,开始缓慢加入聚醚大单体和分散剂水溶液,与此同时缓慢滴加引发剂、分子量调节剂,上述四种原料的加入持续时间控制在90~120分钟,待滴加完毕后,恒温反应4~6h;When the reaction temperature reaches 60 ℃ ~ 75 ℃, start to slowly add polyether macromonomer and dispersant aqueous solution, and at the same time slowly add initiator and molecular weight regulator, the adding duration of the above four raw materials is controlled at 90 ~ 120 minutes, after the dropwise addition is completed, the constant temperature reaction is performed for 4 to 6 hours;
反应结束后,冷却至20℃~30℃,再加入30~35%的氢氧化钠溶液调节pH=6~8,即得减缩型聚羧酸减水剂。After the reaction is completed, it is cooled to 20°C to 30°C, and then 30 to 35% sodium hydroxide solution is added to adjust pH=6 to 8 to obtain a condensation-reducing polycarboxylate water-reducing agent.
作为优选,步骤(1)中,所述莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:5~10:8~18;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2~3:5.5~8.5:3.5~6:2.5~4.5:5.5~7.5。Preferably, in step (1), the weight ratio of the molar salt, maleic anhydride and sodium bisulfite is: 1:5-10:8-18; the sodium bisulfite, sodium persulfate, acrylic acid The weight ratio of the aqueous solution, the aqueous propylene oxide solution, the aqueous solution of isoprenol and the distilled water is 1:2-3:5.5-8.5:3.5-6:2.5-4.5:5.5-7.5.
作为优选,步骤(2)中,所述不饱和羧酸烷基酯包括丙烯酸二甲氨基乙酯、甲基丙烯酸二甲氨基乙酯、丙烯酸二甲氨基丙酯等中的一种或几种按任意配比混合的物质;所述磺酸基单体包括乙烯基磺酸、甲基烯丙基磺酸、异戊二烯磺酸、3-烯丙氧基-2-羟基丙磺酸、丙烯酰胺-2-甲基丙磺酸以及这些酸的盐中的一种或几种按任意配比混合的物质。Preferably, in step (2), the unsaturated carboxylic acid alkyl ester includes one or more of dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate, dimethylaminopropyl acrylate, etc. Mixed substances in any proportion; the sulfonic acid-based monomers include vinyl sulfonic acid, methallyl sulfonic acid, isoprene sulfonic acid, 3-allyloxy-2-hydroxypropane sulfonic acid, propylene One or more of the amide-2-methylpropanesulfonic acid and the salts of these acids are mixed in any proportion.
作为优选,步骤(2)中,所述聚醚大单体包括甲氧基聚乙二醇醚、异戊烯醇聚乙二醇醚、丙烯醇聚乙二醇醚和异丁烯醇聚乙二醇醚中的一种或几种按任意配比混合的物质;所述分散剂为烷基酰胺甜菜碱。Preferably, in step (2), the polyether macromonomer includes methoxy polyethylene glycol ether, prenol polyethylene glycol ether, allyl alcohol polyethylene glycol ether and isobutenol polyethylene glycol One or more of the ethers are mixed in any proportion; the dispersant is an alkylamide betaine.
作为优选,步骤(2)中,所述引发剂包括过氧化氢、过硫酸铵、过氧化苯甲酰、偶氮二异丁酸二甲酯中的一种或几种按任意配比混合的物质;所述分子量调节剂包括巯基乙醇、巯基乙酸、巯基丙酸、异丙醇、十二烷基硫醇中的一种或几种按任意配比混合的物质。Preferably, in step (2), the initiator includes one or more of hydrogen peroxide, ammonium persulfate, benzoyl peroxide, and dimethyl azobisisobutyrate mixed in any proportion. substance; the molecular weight regulator includes one or more substances mixed in any proportion among mercaptoethanol, mercaptoacetic acid, mercaptopropionic acid, isopropanol and dodecyl mercaptan.
作为优选,所述分散剂包括月桂酰胺基丙基甜菜碱、椰油酰胺丙基甜菜碱、十八酰胺基丙基甜菜碱中的一种或几种按任意配比混合和物质。Preferably, the dispersing agent includes one or more of lauramidopropyl betaine, cocamidopropyl betaine, and octadecamidopropyl betaine, mixed and mixed in any proportion.
作为优选,所述磺酸基单体、减缩功能聚合单体、不饱和羧酸烷基酯、聚醚大单体、蒸馏水的重量比为:1:3.5~4.5:1.5~2.5:5.5~10:12~18;优选的,所述磺酸基单体、减缩功能聚合单体、不饱和羧酸烷基酯、聚醚大单体、蒸馏水的重量比为:1:3.8~4.2:1.7~2.1:5.7~9.5:13.6~17.3。Preferably, the weight ratio of the sulfonic acid-based monomer, the shrinkage-reducing functional polymerized monomer, the unsaturated carboxylic acid alkyl ester, the polyether macromonomer, and the distilled water is: 1:3.5-4.5:1.5-2.5:5.5-10 : 12~18; preferably, the weight ratio of the sulfonic acid-based monomer, the shrinkage-reducing functional polymer monomer, the unsaturated carboxylic acid alkyl ester, the polyether macromonomer, and the distilled water is: 1:3.8~4.2:1.7~ 2.1:5.7~9.5:13.6~17.3.
作为优选,所述分散剂用量为聚醚大单体重量的0.5%~2%,所述引发剂用量为聚醚大单体重量的0.2%~0.7%,所述分子量调节剂用量为聚醚大单体重量的0.3%~0.8%;优选的,所述分散剂用量为聚醚大单体重量的0.6%~1.3%,所述引发剂用量为聚醚大单体重量的0.25%~0.41%,所述分子量调节剂用量为聚醚大单体重量的0.34%~0.52%。Preferably, the dosage of the dispersant is 0.5% to 2% of the weight of the polyether macromonomer, the dosage of the initiator is 0.2% to 0.7% of the weight of the polyether macromonomer, and the dosage of the molecular weight regulator is the amount of the polyether macromonomer. 0.3% to 0.8% of the weight of the macromonomer; preferably, the amount of the dispersant is 0.6% to 1.3% of the weight of the polyether macromonomer, and the amount of the initiator is 0.25% to 0.41% of the weight of the polyether macromonomer %, the dosage of the molecular weight regulator is 0.34% to 0.52% of the weight of the polyether macromonomer.
作为优选,步骤(1)中,在反应器中滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。Preferably, in step (1), 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution, 15% sodium persulfate, 15% hydrogen sulfite are added dropwise to the reactor Sodium participates in the reaction as an initiator.
采用上述技术方案后,本发明具有如下优点:After adopting the above-mentioned technical scheme, the present invention has the following advantages:
(1)本发明所述的减缩型聚羧酸减水剂是一种兼备“减缩”和“减水”功能的混凝土外加剂,这种减缩、减水一体化外加剂与水泥其他外加剂均有良好的相容性,具有长期的应用前景;(1) The shrinkage-reducing polycarboxylate water-reducing agent of the present invention is a concrete admixture with both "shrinkage-reducing" and "water-reducing" functions. Good compatibility and long-term application prospects;
(2)本发明所述的减缩型聚羧酸减水剂其分子结构中包含有大量的醇羟基、酰胺、氨基等亲水基团,在聚合过程中会出现交联作用,增加体系的空间位阻效应,这种空间位阻效应使本发明的减水剂在混凝土中具有较好的分散性能,能够均匀的分布在混凝土体系中,不被水泥粒子等吸附在表面;(2) The molecular structure of the shrinkage-reducing polycarboxylate water-reducing agent of the present invention contains a large number of alcoholic hydroxyl groups, amides, amino groups and other hydrophilic groups, and cross-linking occurs during the polymerization process, increasing the space of the system Steric hindrance effect, this steric hindrance effect makes the water reducing agent of the present invention have better dispersing performance in concrete, can be evenly distributed in the concrete system, and is not adsorbed on the surface by cement particles, etc.;
(3)本发明所述的减缩型聚羧酸减水剂仲存在不饱和羧酸烷基酯的结构单体,这种结构单体在混凝土的碱性环境下释放出具有减水功能的羧酸基团,使得本发明最终得到的减水剂具有突出的保坍效果;(3) The shrinkage-reducing polycarboxylate water-reducing agent of the present invention contains a structural monomer of unsaturated carboxylic acid alkyl ester, which releases carboxylate with water-reducing function in the alkaline environment of concrete. acid group, so that the water reducing agent finally obtained by the present invention has outstanding slump retention effect;
(4)本发明所述的减缩型聚羧酸减水剂中存在亚烷基二醇/烯基醚/马来酸酐结构单元,此结构单元作为一种表面活性有效成分,贡献出应有的减缩功能,因其能够降低混凝土毛细管中液相的表面张力,使毛细管中的负压下降,减少收缩应力,从而有效降低了混凝土的收缩率;(4) There is an alkylene glycol/alkenyl ether/maleic anhydride structural unit in the shrinkage-reducing polycarboxylate water-reducing agent of the present invention, and this structural unit, as a surface active active ingredient, contributes due The shrinkage reduction function, because it can reduce the surface tension of the liquid phase in the concrete capillary, reduce the negative pressure in the capillary, reduce the shrinkage stress, and effectively reduce the shrinkage rate of the concrete;
(5)本发明所述的减缩型聚羧酸减水剂的减缩、减水功效受温度的影响较小,加入到混凝土中后,能降低水泥的水化热,但不妨碍水泥的正常水化,且在一定时间内能够保持水泥浆体的良好塑性;(5) The shrinkage-reducing and water-reducing effects of the shrinkage-reducing polycarboxylate water-reducing agent of the present invention are less affected by temperature. After being added to concrete, it can reduce the heat of hydration of cement, but does not hinder the normal water content of cement. It can maintain the good plasticity of the cement paste within a certain period of time;
(6)本发明所述的减缩型聚羧酸减水剂能达到环保要求,具有低挥发性且无异常的引起作用,能够保证混凝土应有的强度要求,不易受酸、碱物质的影响,作为一种外加剂,在混凝土中的掺量较低,原料易得,合成工艺清晰。(6) The shrinkage-reducing polycarboxylate water-reducing agent of the present invention can meet the requirements of environmental protection, has low volatility and no abnormal causing effect, can ensure the required strength of concrete, and is not easily affected by acids and alkalis. As an admixture, the dosage in concrete is low, the raw materials are readily available, and the synthesis process is clear.
具体实施方式Detailed ways
一种减缩型聚羧酸减水剂,包括以下结构的有效组分:A shrinkage-reducing polycarboxylate water-reducing agent, comprising the effective components of the following structure:
; ;
其中,a、b、c、d、x、y和z均为整数,且a=1~30,b=10~65,c=1~25,d=1~18,x=1~32,且x代表氧化烯基团(—R7—O—)的平均加成摩尔数,y=1~20,且y代表氧化烯基团(—R8—O—)的平均加成摩尔数,z=5~27;Among them, a, b, c, d, x, y and z are all integers, and a=1~30, b=10~65, c=1~25, d=1~18, x=1~32, And x represents the average added moles of oxyalkylene groups (—R7—O—), y=1~20, and y represents the average added moles of oxyalkylene groups (—R8—O—), z= 5~27;
R1和R2为—H或—CH3,R3为1~2个碳的烷基,R4为—H或1~2个碳的烷基,R5为—H或—CH3,R6为1~2个碳的烷基,R7为C2~C20的亚烷基,R8为C2~C4的亚烷基,R9为—H或2~3个碳的烷基,A为C1~C3的亚烷基,M为Na或K或NH4。R1 and R2 are -H or -CH3, R3 is an alkyl group of 1-2 carbons, R4 is -H or an alkyl group of 1-2 carbons, R5 is -H or -CH3, R6 is 1-2 carbons R7 is C2~C20 alkylene, R8 is C2~C4 alkylene, R9 is -H or 2~3 carbon alkyl, A is C1~C3 alkylene, M is C1~C3 alkylene Na or K or NH4.
以下结合具体实施例,对上述减缩型聚羧酸减水剂的制备方法作进一步的详细说明。The preparation method of the above-mentioned shrinkage-reducing polycarboxylate water-reducing agent will be further described in detail below with reference to specific examples.
实施例1Example 1
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到70℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为75分钟、80分钟、70分钟、70分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化40分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:5:11;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2:6:3.5:4:5.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 70°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 75 minutes, 80 minutes, 70 minutes and 70 minutes. Take the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 40 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride and sodium bisulfite is: 1:5:11; the sodium bisulfite, sodium persulfate, acrylic acid aqueous solution, cyclic The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2:6:3.5:4:5.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至42℃,搅拌25分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和异戊二烯磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到65℃时开始缓慢加入分子量为3000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在112分钟,待滴加完毕后,恒温反应5h,其中所述异戊二烯磺酸、减缩功能聚合单体、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4:2.1:9.5:16.4,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的1.1%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.28%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.46%。反应结束后,冷却至25℃,再加入32%的氢氧化钠溶液调节pH=7.2,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 42 ℃, stir for 25 minutes, add dimethylaminoethyl acrylate and isoprene sulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, and start slowly when the reaction temperature reaches 65 ℃ Add the prenyl alcohol polyglycol ether and the lauryl amidopropyl betaine aqueous solution that the molecular weight is 3000, slowly drip ammonium persulfate and mercaptopropionic acid at the same time, the adding duration of the above-mentioned four kinds of raw materials is controlled at 112 minutes , after the dropwise addition is completed, the constant temperature reaction is performed for 5h, wherein the weight ratio of the isoprene sulfonic acid, the shrinkage-reducing functional polymerization monomer, dimethylaminoethyl acrylate, the prenol polyglycol ether, and the distilled water is: 1:4:2.1:9.5:16.4, the amount of lauramidopropyl betaine is 1.1% of the weight of prenol polyethylene glycol ether, and the amount of ammonium persulfate is prenol polyethylene glycol 0.28% of the weight of the ether, and the amount of the mercaptopropionic acid used is 0.46% of the weight of the prenol polyethylene glycol ether. After the reaction is completed, it is cooled to 25° C., and then 32% sodium hydroxide solution is added to adjust pH=7.2 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例2Example 2
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到75℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为70分钟、75分钟、70分钟、75分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化42分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:8:10;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.4:6.8:5.1:3.8:7.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 75°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 70 minutes, 75 minutes, 70 minutes and 75 minutes. Adopt the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 42 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:8:10; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.4:6.8:5.1:3.8:7.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至40℃,搅拌27分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和乙烯基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到70℃时开始缓慢加入分子量为2000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述乙烯基磺酸、减缩功能聚合单体、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:3.5:1.5:6.2:18,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的2%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.7%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.69%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6.8,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 40 ℃, stir for 27 minutes, add dimethylaminoethyl acrylate and vinyl sulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 70 ℃, slowly add molecular weight Be 2000 of isoprenol polyglycol ether and lauryl amidopropyl betaine aqueous solution, slowly drip ammonium persulfate and mercaptopropionic acid at the same time, the adding duration of above-mentioned four kinds of raw materials is controlled at 105 minutes, wait for After the dropwise addition, the constant temperature reaction was carried out for 5.5h, wherein the weight ratio of vinyl sulfonic acid, shrinkage-reducing functional polymer monomer, dimethylaminoethyl acrylate, prenol polyglycol ether, and distilled water was: 1:3.5 : 1.5:6.2:18, the described lauryl amidopropyl betaine consumption is 2% of the prenol polyglycol ether weight, and the described ammonium persulfate consumption is the prenol polyglycol ether weight of 2%. 0.7%, the mercaptopropionic acid consumption is 0.69% by weight of the prenol polyglycol ether. After the reaction is completed, it is cooled to 26° C., and then 32% sodium hydroxide solution is added to adjust pH=6.8 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例3Example 3
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到80℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为70分钟、75分钟、70分钟、75分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化42分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:8:10;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.4:6.8:5.5:3.8:7.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, Mohr salt and maleic anhydride, and heat to 80°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 70 minutes, 75 minutes, 70 minutes and 75 minutes. Adopt the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 42 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:8:10; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.4:6.8:5.5:3.8:7.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至40℃,搅拌30分钟,待其混合均匀后加入甲基丙烯酸二甲氨基乙酯和甲基烯丙基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到75℃时开始缓慢加入分子量为2000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述甲基烯丙基磺酸、减缩功能聚合单体、甲基丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4.2:2.1:6.2:17.3,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的0.5%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.2%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.35%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 40°C, stir for 30 minutes, add dimethylaminoethyl methacrylate and methallyl sulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 75°C Begin to slowly add isoprenol polyglycol ether and lauryl amidopropyl betaine aqueous solution that molecular weight is 2000, slowly drip ammonium persulfate, mercaptopropionic acid simultaneously, the adding duration control of above-mentioned four kinds of raw materials At 105 minutes, after the dropwise addition is completed, a constant temperature reaction is performed for 5.5 hours, wherein the methallyl sulfonic acid, the shrinkage-reducing functional polymer monomer, dimethylaminoethyl methacrylate, and the prenol polyglycol ether , the weight ratio of distilled water is: 1:4.2:2.1:6.2:17.3, the described lauryl amidopropyl betaine consumption is 0.5% of the prenol polyglycol ether weight, and the described ammonium persulfate consumption is different. 0.2% of the weight of the pentenol polyethylene glycol ether, and the amount of the mercaptopropionic acid is 0.35% of the weight of the prenol polyethylene glycol ether. After the reaction is completed, it is cooled to 26° C., and then 32% sodium hydroxide solution is added to adjust pH=6 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例4Example 4
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到75℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为77分钟、73分钟、73分钟、77分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化45分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:7.6:15;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.8:7.8:5.1:3.6:7.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 75°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate, and sodium bisulfite were 77 minutes, 73 minutes, 73 minutes, and 77 minutes, respectively. Take the method of dropping the above-mentioned various solutions at the same time. After the dropping is completed, the obtained solution is further matured for 45 minutes at the same controlled temperature. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:7.6:15; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.8:7.8:5.1:3.6:7.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至45℃,搅拌30分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和乙烯基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到70℃时开始缓慢加入分子量为2000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述乙烯基磺酸、减缩功能聚合单体、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:3.9:1.9:5.5:12,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的1.3%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.35%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.41%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6.5,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 45°C, stir for 30 minutes, add dimethylaminoethyl acrylate and vinylsulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 70°C, slowly add molecular weight Be 2000 of isoprenol polyglycol ether and lauryl amidopropyl betaine aqueous solution, slowly drip ammonium persulfate and mercaptopropionic acid at the same time, the adding duration of above-mentioned four kinds of raw materials is controlled at 105 minutes, wait for After the dropwise addition, the constant temperature reaction was carried out for 5.5 hours, wherein the weight ratio of vinyl sulfonic acid, shrinkage-reducing functional polymerization monomer, dimethylaminoethyl acrylate, prenol polyglycol ether, and distilled water was: 1:3.9 : 1.9:5.5:12, the described lauryl amidopropyl betaine consumption is 1.3% of the weight of prenol polyglycol ether, and the described ammonium persulfate consumption is 1.3% of the weight of prenol polyglycol ether. 0.35%, the mercaptopropionic acid consumption is 0.41% by weight of the prenol polyglycol ether. After the reaction is completed, it is cooled to 26° C., and then 32% sodium hydroxide solution is added to adjust pH=6.5 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例5Example 5
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到75℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为75分钟、73分钟、76分钟、74分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化40分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:8.8:18;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:3:8.2:5.5:3.8:7.1。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 75°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 75 minutes, 73 minutes, 76 minutes and 74 minutes. Take the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 40 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride and sodium bisulfite is: 1:8.8:18; the sodium bisulfite, sodium persulfate, acrylic acid aqueous solution, cyclic The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:3:8.2:5.5:3.8:7.1.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至42℃,搅拌30分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和甲基烯丙基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到70℃时开始缓慢加入分子量为4000的丙烯醇聚乙二醇醚和椰油酰胺丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述甲基烯丙基磺酸、减缩功能聚合单体、丙烯酸二甲氨基乙酯、丙烯醇聚乙二醇醚、蒸馏水的重量比为:1:3.9:1.9:6.2:17.3,所述椰油酰胺丙基甜菜碱用量为丙烯醇聚乙二醇醚重量的1.3%,所述过硫酸铵用量为丙烯醇聚乙二醇醚重量的0.35%,所述巯基丙酸用量为丙烯醇聚乙二醇醚重量的0.8%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6.8,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 42 °C, stir for 30 minutes, add dimethylaminoethyl acrylate and methallyl sulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, start when the reaction temperature reaches 70 °C Slowly adding molecular weight is 4000 propenyl alcohol polyglycol ether and cocamidopropyl betaine aqueous solution, slowly dripping ammonium persulfate, mercaptopropionic acid simultaneously, the adding duration of above-mentioned four kinds of raw materials is controlled at 105 minutes, After the dropwise addition is completed, the constant temperature reaction is carried out for 5.5h, wherein the weight ratio of the methallyl sulfonic acid, the shrinkage-reducing functional polymer monomer, the dimethylaminoethyl acrylate, the propylene alcohol polyethylene glycol ether, and the distilled water is: 1 : 3.9: 1.9: 6.2: 17.3, the cocamidopropyl betaine consumption is 1.3% of the propenyl alcohol polyglycol ether weight, and the described ammonium persulfate consumption is 0.35% of the propenyl alcohol polyglycol ether weight , the amount of mercaptopropionic acid is 0.8% of the weight of propylene alcohol polyethylene glycol ether. After the reaction is completed, it is cooled to 26° C., and then 32% sodium hydroxide solution is added to adjust pH=6.8 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例6Example 6
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到70℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为75分钟、80分钟、70分钟、70分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化40分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:10:17.3;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为: 1:3:8.5:5:4:6.8。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 70°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 75 minutes, 80 minutes, 70 minutes and 70 minutes. Take the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 40 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:10:17.3; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is: 1:3:8.5:5:4:6.8.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至42℃,搅拌25分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和甲基烯丙基磺酸钠,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到65℃时开始缓慢加入分子量为3000的异戊烯醇聚乙二醇醚和椰油酰胺丙基甜菜碱水溶液,与此同时缓慢滴加过氧化氢、巯基丙酸,上述四种原料的加入持续时间控制在120分钟,待滴加完毕后,恒温反应6h,其中所述甲基烯丙基磺酸钠、减缩功能聚合单体、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4:2:8.2:16.8,所述椰油酰胺丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的1.3%,所述过氧化氢用量为异戊烯醇聚乙二醇醚重量的0.4%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.52%。反应结束后,冷却至20℃,再加入32%的氢氧化钠溶液调节pH=7.5,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 42°C, stir for 25 minutes, add dimethylaminoethyl acrylate and sodium methallyl sulfonate after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 65°C Begin to slowly add the isoprenol polyglycol ether and cocamidopropyl betaine aqueous solution that molecular weight is 3000, slowly drip hydrogen peroxide, mercaptopropionic acid simultaneously, the adding duration of above-mentioned four kinds of raw materials is controlled at 120 minutes, after the dropwise addition is completed, a constant temperature reaction is performed for 6 hours, wherein the sodium methallyl sulfonate, the shrinkage-reducing functional polymer monomer, dimethylaminoethyl acrylate, the prenol polyglycol ether, and distilled water are mixed. The weight ratio is: 1:4:2:8.2:16.8, the cocamidopropyl betaine consumption is 1.3% of the prenol polyglycol ether weight, and the hydrogen peroxide consumption is prenol 0.4% of the weight of the polyethylene glycol ether, and the amount of the mercaptopropionic acid is 0.52% of the weight of the prenol polyethylene glycol ether. After the reaction is completed, it is cooled to 20° C., and then 32% sodium hydroxide solution is added to adjust pH=7.5 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例7Example 7
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到80℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为72分钟、75分钟、75分钟、77分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化42分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:7.1:14.9;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.4:6.9:5.5:4.5:6.3。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, Mohr salt and maleic anhydride, and heat to 80°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 72 minutes, 75 minutes, 75 minutes and 77 minutes. Adopt the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 42 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:7.1:14.9; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.4:6.9:5.5:4.5:6.3.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至42℃,搅拌24分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和甲基烯丙基磺酸钠,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到75℃时开始缓慢加入分子量为4000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基乙酸,上述四种原料的加入持续时间控制在112分钟,待滴加完毕后,恒温反应5.5h,其中所述甲基烯丙基磺酸钠、减缩功能聚合单体、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4.1:1.9:8.2:15.9,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的0.9%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.37%,所述巯基乙酸用量为异戊烯醇聚乙二醇醚重量的0.5%。反应结束后,冷却至30℃,再加入32%的氢氧化钠溶液调节pH=7.3,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 42°C, stir for 24 minutes, add dimethylaminoethyl acrylate and sodium methallyl sulfonate after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 75°C Begin to slowly add the isoprenol polyglycol ether and lauramidopropyl betaine aqueous solution that molecular weight is 4000, slowly drip ammonium persulfate, mercaptoacetic acid simultaneously, the adding duration of above-mentioned four kinds of raw materials is controlled at 112 minutes, after the dropwise addition is completed, a constant temperature reaction is performed for 5.5 hours, wherein the sodium methallyl sulfonate, the shrinkage-reducing functional polymer monomer, dimethylaminoethyl acrylate, the prenol polyglycol ether, and distilled water are mixed The weight ratio is: 1:4.1:1.9:8.2:15.9, the lauryl amidopropyl betaine consumption is 0.9% of the weight of prenol polyglycol ether, and the ammonium persulfate consumption is prenol 0.37% by weight of polyethylene glycol ether, and the amount of thioglycolic acid used is 0.5% by weight of prenol polyethylene glycol ether. After the reaction is completed, it is cooled to 30° C., and then 32% sodium hydroxide solution is added to adjust pH=7.3 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
实施例8Example 8
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到60℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为72分钟、75分钟、75分钟、77分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化70分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:5:8;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.4:5.5:6:2.5:6.3。(1) Preparation of polymerized monomers with shrinkage reduction function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 60°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 72 minutes, 75 minutes, 75 minutes and 77 minutes. Adopt the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 70 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:5:8; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.4:5.5:6:2.5:6.3.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至35℃,搅拌10分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和甲基烯丙基磺酸钠,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到60℃时开始缓慢加入分子量为4000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基乙酸,上述四种原料的加入持续时间控制在90分钟,待滴加完毕后,恒温反应4h,其中所述甲基烯丙基磺酸钠、减缩功能聚合单体、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4.5:2.5:10:15.9,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的0.9%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.42%,所述巯基乙酸用量为异戊烯醇聚乙二醇醚重量的0.3%。反应结束后,冷却至28℃,再加入32%的氢氧化钠溶液调节pH=8,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 35 ℃, stir for 10 minutes, add dimethylaminoethyl acrylate and sodium methallyl sulfonate after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 60 ℃ Begin to slowly add the isoprenol polyglycol ether and lauramidopropyl betaine aqueous solution that molecular weight is 4000, slowly drip ammonium persulfate, mercaptoacetic acid simultaneously, the adding duration of above-mentioned four kinds of raw materials is controlled at 90 minutes, after the dropwise addition is completed, a constant temperature reaction is performed for 4 hours, wherein the weight of the sodium methallyl sulfonate, the shrinkage-reducing functional polymer monomer, dimethylaminoethyl acrylate, the prenol polyglycol ether, and distilled water The ratio is: 1:4.5:2.5:10:15.9, the consumption of the lauryl amidopropyl betaine is 0.9% of the weight of the prenol polyglycol ether, and the consumption of the ammonium persulfate is the prenol polyglycol ether. 0.42% of the weight of the glycol ether, and the amount of the thioglycolic acid used is 0.3% of the weight of the prenol polyglycol ether. After the reaction is completed, it is cooled to 28° C., and then 32% sodium hydroxide solution is added to adjust pH=8 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
对比例1Comparative Example 1
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到70℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为75分钟、80分钟、70分钟、70分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化40分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:5:11;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2:6:3.5:4:5.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 70°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 75 minutes, 80 minutes, 70 minutes and 70 minutes. Take the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 40 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride and sodium bisulfite is: 1:5:11; the sodium bisulfite, sodium persulfate, acrylic acid aqueous solution, cyclic The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is: 1:2:6:3.5:4:5.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至42℃,搅拌25分钟,待其混合均匀后加入丙烯酸二甲氨基丙酯和丙烯酰胺-2-甲基丙磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到65℃时开始缓慢加入分子量为3000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在112分钟,待滴加完毕后,恒温反应5h,其中所述丙烯酰胺-2-甲基丙磺酸、减缩功能聚合单体、丙烯酸二甲氨基丙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4:2.1:9.5:16.4,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的1.1%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.28%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.46%。反应结束后,冷却至25℃,再加入32%的氢氧化钠溶液调节pH=7.2,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 42°C, stir for 25 minutes, add dimethylaminopropyl acrylate and acrylamide-2-methylpropanesulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 65 At ℃, start to slowly add isoprenol polyglycol ether and lauramidopropyl betaine aqueous solution with a molecular weight of 3000, and at the same time slowly add ammonium persulfate and mercaptopropionic acid dropwise, and the duration of the addition of the above four raw materials Controlled at 112 minutes, after the dropwise addition was completed, a constant temperature reaction was performed for 5 hours, wherein the acrylamide-2-methylpropanesulfonic acid, shrinkage-reducing functional polymer monomer, dimethylaminopropyl acrylate, and prenol polyethylene glycol The weight ratio of ether and distilled water is: 1:4:2.1:9.5:16.4, the lauryl amidopropyl betaine consumption is 1.1% of the prenol polyglycol ether weight, and the ammonium persulfate consumption is 0.28% of the weight of the prenol polyglycol ether, and the amount of the mercaptopropionic acid is 0.46% of the weight of the prenol polyglycol ether. After the reaction is completed, it is cooled to 25° C., and then 32% sodium hydroxide solution is added to adjust pH=7.2 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
对比例2Comparative Example 2
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到75℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为70分钟、75分钟、70分钟、75分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化42分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:8:10;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.4:6.8:5.1:3.8:7.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, molar salt and maleic anhydride, and heat to 75°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 70 minutes, 75 minutes, 70 minutes and 75 minutes. Adopt the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 42 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:8:10; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.4:6.8:5.1:3.8:7.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至40℃,搅拌27分钟,待其混合均匀后加入乙烯基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到70℃时开始缓慢加入分子量为2000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述乙烯基磺酸、减缩功能聚合单体、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:3.9:6.2:17.3,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的1.3%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.35%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.41%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6.8,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 40 ° C, stir for 27 minutes, add vinyl sulfonic acid after mixing it evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 70 ° C, slowly add prenol with a molecular weight of 2000 Polyethylene glycol ether and lauramidopropyl betaine aqueous solution, at the same time, slowly add ammonium persulfate and mercaptopropionic acid dropwise, the duration of adding the above four raw materials is controlled at 105 minutes, after the dropwise addition, the constant temperature reaction 5.5h, wherein the weight ratio of vinyl sulfonic acid, shrinkage-reducing functional polymer monomer, prenol polyglycol ether, and distilled water is: 1:3.9:6.2:17.3, and the lauroamidopropyl betaine Consumption is 1.3% by weight of prenol polyethylene glycol ether, described ammonium persulfate consumption is 0.35% by weight of prenol polyglycol ether, and described mercaptopropionic acid consumption is prenol polyethylene glycol ether 0.41% by weight of glycol ether. After the reaction is completed, it is cooled to 26° C., and then 32% sodium hydroxide solution is added to adjust pH=6.8 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
对比例3Comparative Example 3
一种减缩型聚羧酸减水剂及其制备方法,通过如下步骤实现:A shrinkage-reducing polycarboxylate water-reducing agent and a preparation method thereof are realized by the following steps:
(1)减缩功能聚合单体的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,加入蒸馏水、莫尔盐和马来酸酐,同时加热到80℃,向所述混合物中通过不同的开口分别滴加72%丙烯酸水溶液、75%环氧丙烷水溶液、55%异戊二烯醇水溶液,外加15%的过硫酸钠、15%的亚硫酸氢钠作为引发剂参与反应。其中丙烯酸、环氧丙烷、过硫酸钠、亚硫酸氢钠的滴加时间分别为70分钟、75分钟、70分钟、75分钟。采取同时滴加上述各种溶液的方式,待滴加完成后,将所得溶液在相同的受控温度下再熟化42分钟,反应结束后静置冷却,通过以上步骤得到亚烷基二醇/烯基醚/马来酸酐减缩功能共聚物,其中莫尔盐、马来酸酐、亚硫酸氢钠的重量比为:1:8:10;所述亚硫酸氢钠、过硫酸钠、丙烯酸水溶液、环氧丙烷水溶液、异戊二烯醇水溶液、蒸馏水的重量比为:1:2.4:6.8:5.5:3.8:7.5。(1) Preparation of polymerized monomer with shrinkage-reducing function: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water, Mohr salt and maleic anhydride, and heat to 80°C at the same time , 72% acrylic acid aqueous solution, 75% propylene oxide aqueous solution, 55% isoprenol aqueous solution were added dropwise through different openings in the mixture, and 15% sodium persulfate and 15% sodium bisulfite were added as The initiator participates in the reaction. The dropwise addition times of acrylic acid, propylene oxide, sodium persulfate and sodium bisulfite were respectively 70 minutes, 75 minutes, 70 minutes and 75 minutes. Adopt the mode of dropping the above-mentioned various solutions at the same time, after the dropping is completed, the obtained solution is further matured for 42 minutes at the same controlled temperature, and after the reaction is completed, it is allowed to stand for cooling, and the alkylene glycol/alkene is obtained through the above steps. Base ether/maleic anhydride shrinkage-reducing functional copolymer, wherein the weight ratio of molar salt, maleic anhydride, and sodium bisulfite is: 1:8:10; The weight ratio of the oxypropane aqueous solution, the isoprenol aqueous solution and the distilled water is 1:2.4:6.8:5.5:3.8:7.5.
(2)减缩型聚羧酸减水剂的制备:在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入减缩功能聚合单体和蒸馏水,升温至40℃,搅拌30分钟,待其混合均匀后加入甲基丙烯酸二甲氨基乙酯和甲基烯丙基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到75℃时开始缓慢加入分子量为2000的异戊烯醇聚乙二醇醚,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述甲基烯丙基磺酸、减缩功能聚合单体、甲基丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:4.2:2.1:6.2:17.3,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.35%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.41%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6.8,即得减缩型聚羧酸减水剂。(2) Preparation of shrinkage-reducing polycarboxylate water-reducing agent: In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked bottle, add the shrinkage-reducing functional polymer monomer and distilled water into the four-necked bottle. , heat up to 40°C, stir for 30 minutes, add dimethylaminoethyl methacrylate and methallyl sulfonic acid after mixing evenly, under nitrogen protection, heat and stir in a constant temperature water bath, when the reaction temperature reaches 75°C Begin to slowly add isoprenol polyglycol ether with a molecular weight of 2000 at the same time, and slowly add ammonium persulfate and mercaptopropionic acid dropwise at the same time. , constant temperature reaction 5.5h, wherein the weight ratio of described methallyl sulfonic acid, shrinkage-reducing functional polymerization monomer, dimethylaminoethyl methacrylate, prenyl polyglycol ether, distilled water is: 1: 4.2:2.1:6.2:17.3, the amount of the ammonium persulfate is 0.35% by weight of the prenol polyglycol ether, and the amount of the mercaptopropionic acid is 0.41% by the weight of the prenol polyglycol ether. After the reaction is completed, it is cooled to 26° C., and then 32% sodium hydroxide solution is added to adjust pH=6.8 to obtain a shrinkage-reducing polycarboxylate water-reducing agent.
对比例4Comparative Example 4
一种不另掺减缩功能单体的聚羧酸减水剂及其制备方法,通过如下步骤实现:A polycarboxylate water-reducing agent without additional shrinkage-reducing functional monomers and a preparation method thereof are realized by the following steps:
在配有回流冷凝管和搅拌器以及四口瓶的可拆式控温反应器中,往四口瓶中加入蒸馏水,升温至44℃,搅拌30分钟,待其混合均匀后加入丙烯酸二甲氨基乙酯和乙烯基磺酸,在氮气保护下,恒温水浴加热并搅拌,当反应温度达到70℃时开始缓慢加入分子量为2000的异戊烯醇聚乙二醇醚和月桂酰胺基丙基甜菜碱水溶液,与此同时缓慢滴加过硫酸铵、巯基丙酸,上述四种原料的加入持续时间控制在105分钟,待滴加完毕后,恒温反应5.5h,其中所述乙烯基磺酸、丙烯酸二甲氨基乙酯、异戊烯醇聚乙二醇醚、蒸馏水的重量比为:1:1.9:6.2:17.3,所述月桂酰胺基丙基甜菜碱用量为异戊烯醇聚乙二醇醚重量的1.3%,所述过硫酸铵用量为异戊烯醇聚乙二醇醚重量的0.35%,所述巯基丙酸用量为异戊烯醇聚乙二醇醚重量的0.41%。反应结束后,冷却至26℃,再加入32%的氢氧化钠溶液调节pH=6.5,即得不另掺减缩功能单体的聚羧酸减水剂。In a detachable temperature-controlled reactor equipped with a reflux condenser, agitator and a four-necked flask, add distilled water to the four-necked flask, raise the temperature to 44°C, stir for 30 minutes, and add dimethylamino acrylate after mixing evenly. Ethyl ester and vinyl sulfonic acid were heated and stirred in a constant temperature water bath under the protection of nitrogen. When the reaction temperature reached 70 °C, the prenyl polyglycol ether with a molecular weight of 2000 and lauroamidopropyl betaine were slowly added. Aqueous solution, at the same time, ammonium persulfate and mercaptopropionic acid were slowly added dropwise, and the addition duration of the above four raw materials was controlled at 105 minutes. The weight ratio of methylaminoethyl ester, prenol polyglycol ether, distilled water is: 1:1.9:6.2:17.3, and the described lauroamidopropyl betaine consumption is the weight of prenol polyglycol ether 1.3% of the ammonium persulfate, the amount of the ammonium persulfate is 0.35% of the weight of the prenol polyglycol ether, and the amount of the mercaptopropionic acid is 0.41% of the weight of the prenol polyglycol ether. After the reaction is completed, it is cooled to 26°C, and then 32% sodium hydroxide solution is added to adjust pH=6.5, that is, a polycarboxylate water-reducing agent without additional shrinkage-reducing functional monomer is obtained.
性能测试Performance Testing
根据GB/T-8077-2012《混凝土外加剂均质性实验方法》、JC/T2361-2016《砂浆、混凝土减缩剂》、JC/T603-2008《水泥胶砂干缩实验方法》等的有关规定,对实施例1-7及对比例1-4进行性能测试,其抗压强度按照GB/T5008-2016《普通混凝土力学性能试验方法标准》进行。原料中水泥选用市售P•O 32.5级,河砂细度模数为2.5,碎石为5~20mm的连续级配碎石,固定水灰比为0.29,减缩型聚羧酸减水剂掺量为胶凝材料总质量的1.2%,空白对照组为不加本发明减缩型聚羧酸减水剂的混凝土,空白对照的其他掺量与实施例组同。最终测试结果如下表所示。According to GB/T-8077-2012 "Concrete Admixture Homogeneity Test Method", JC/T2361-2016 "Mortar, Concrete Shrinkage Reducer", JC/T603-2008 "Cement Mortar Dry Shrinkage Test Method" and other relevant regulations , The performance tests of Examples 1-7 and Comparative Examples 1-4 were carried out, and their compressive strengths were carried out in accordance with GB/T5008-2016 "Standards for Test Methods of Mechanical Properties of Ordinary Concrete". The cement in the raw materials is commercially available P•O 32.5 grade, the fineness modulus of river sand is 2.5, the crushed stone is continuous graded crushed stone of 5~20mm, the fixed water-cement ratio is 0.29, and the shrinkage-reducing polycarboxylate water-reducing agent is mixed with The amount is 1.2% of the total mass of the cementitious material. The blank control group is the concrete without the shrinkage-reducing polycarboxylate water-reducing agent of the present invention. Other dosages of the blank control are the same as those of the example group. The final test results are shown in the table below.
从上述混凝土的性能测试数据中,整体来看C30混凝土在掺入此减缩型聚羧酸减水剂后后,混凝土抗压强度在7d和28d都有一定程度的增长,这是由于此减缩型聚羧酸减水剂分子结构中包含有大量的醇羟基、酰胺、氨基等亲水基团,在聚合过程中会出现交联作用,增加体系的空间位阻效应,这种空间位阻效应使本发明的减水剂在混凝土中具有较好的分散性能,在混凝土体系中能更好的分散水泥颗粒,充分激发水泥颗粒进行水化作用,提高了水泥的利用率,从而混凝土各龄期强度有所增加;从实施例1-8可知,聚羧酸减水剂分子结构中引入了具有减缩功能的亚烷基二醇/烯基醚/马来酸酐结构单元后,此结构单元作为一种表面活性有效成分,贡献出应有的减缩功能,能够降低混凝土毛细管中液相的表面张力,使毛细管中的负压下降,减少收缩应力,从而有效降低了混凝土的收缩率以及体系的表面张力,而没有引入减缩功能结构单元的对比例4,其相应的减缩效果及表面张力相对于空白组均没有明显的改善;从对比例1-3可知,合成减缩型聚羧酸减水剂的原料的最优选择非常关键,且缺少任何一种原料对最终表现出来的抗压强度、保坍效果、减缩效果等都会带来一定的影响。From the performance test data of the above concrete, as a whole, after adding this shrinkage-reducing polycarboxylate superplasticizer, the compressive strength of the concrete increases to a certain extent at 7d and 28d. This is due to this shrinkage-reducing type. The molecular structure of polycarboxylate superplasticizer contains a large number of hydrophilic groups such as alcoholic hydroxyl groups, amides, and amino groups. During the polymerization process, there will be a cross-linking effect, which increases the steric hindrance effect of the system. This steric hindrance effect makes The water reducing agent of the invention has good dispersing performance in concrete, can better disperse the cement particles in the concrete system, fully stimulate the hydration of the cement particles, improve the utilization rate of the cement, so that the strength of the concrete at each age is improved. It can be seen from Examples 1-8 that after the alkylene glycol/alkenyl ether/maleic anhydride structural unit with shrinkage-reducing function is introduced into the molecular structure of the polycarboxylate water-reducing agent, this structural unit acts as a kind of The surface active active ingredients contribute to the shrinking function, which can reduce the surface tension of the liquid phase in the concrete capillary, reduce the negative pressure in the capillary, and reduce the shrinkage stress, thereby effectively reducing the shrinkage of concrete and the surface tension of the system. However, in Comparative Example 4, which did not introduce shrinkage-reducing functional structural units, its corresponding shrinkage-reducing effect and surface tension were not significantly improved compared to the blank group. The optimal choice is very critical, and the lack of any raw material will have a certain impact on the final compressive strength, slump retention effect, and shrinkage reduction effect.
除上述优选实施例外,本发明还有其他的实施方式,本领域技术人员可以根据本发明作出各种改变和变形,只要不脱离本发明的精神,均应属于本发明所附权利要求所定义的范围。In addition to the above-mentioned preferred embodiments, the present invention also has other embodiments, and those skilled in the art can make various changes and modifications according to the present invention, as long as they do not depart from the spirit of the present invention, they shall all belong to the definition of the appended claims of the present invention scope.
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