CN106883354A - A kind of powdery polycarboxylic-acid slump retaining agent and preparation method thereof - Google Patents
A kind of powdery polycarboxylic-acid slump retaining agent and preparation method thereof Download PDFInfo
- Publication number
- CN106883354A CN106883354A CN201710127466.1A CN201710127466A CN106883354A CN 106883354 A CN106883354 A CN 106883354A CN 201710127466 A CN201710127466 A CN 201710127466A CN 106883354 A CN106883354 A CN 106883354A
- Authority
- CN
- China
- Prior art keywords
- slump
- acid
- retaining agent
- polycarboxylate
- preparation
- 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.)
- Pending
Links
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 66
- 238000002360 preparation method Methods 0.000 title claims abstract description 49
- 239000002253 acid Substances 0.000 title claims abstract description 21
- 229920005646 polycarboxylate Polymers 0.000 claims abstract description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 239000000178 monomer Substances 0.000 claims abstract description 36
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 24
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000003999 initiator Substances 0.000 claims abstract description 22
- 150000002148 esters Chemical class 0.000 claims abstract description 21
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims abstract description 17
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000012986 chain transfer agent Substances 0.000 claims abstract description 10
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 9
- 229920000570 polyether Polymers 0.000 claims abstract description 9
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 claims abstract description 8
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims abstract description 7
- 150000008065 acid anhydrides Chemical class 0.000 claims abstract description 7
- 239000002131 composite material Substances 0.000 claims abstract description 7
- 230000009471 action Effects 0.000 claims abstract description 6
- 239000003054 catalyst Substances 0.000 claims abstract description 6
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 5
- 238000010298 pulverizing process Methods 0.000 claims abstract description 4
- 150000005846 sugar alcohols Polymers 0.000 claims abstract description 4
- 238000007334 copolymerization reaction Methods 0.000 claims abstract description 3
- 238000003756 stirring Methods 0.000 claims description 56
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 18
- 239000000843 powder Substances 0.000 claims description 17
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 14
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 14
- 239000003513 alkali Substances 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 239000011259 mixed solution Substances 0.000 claims description 11
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 claims description 10
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 10
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 10
- DMBHHRLKUKUOEG-UHFFFAOYSA-N diphenylamine Chemical compound C=1C=CC=CC=1NC1=CC=CC=C1 DMBHHRLKUKUOEG-UHFFFAOYSA-N 0.000 claims description 10
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N 1,4-Benzenediol Natural products OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 claims description 9
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 9
- QVDTXNVYSHVCGW-ONEGZZNKSA-N isopentenol Chemical compound CC(C)\C=C\O QVDTXNVYSHVCGW-ONEGZZNKSA-N 0.000 claims description 9
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 8
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical compound CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 claims description 8
- JOXIMZWYDAKGHI-UHFFFAOYSA-N p-toluenesulfonic acid Substances CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 claims description 8
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical group N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 6
- BYDRTKVGBRTTIT-UHFFFAOYSA-N 2-methylprop-2-en-1-ol Chemical group CC(=C)CO BYDRTKVGBRTTIT-UHFFFAOYSA-N 0.000 claims description 6
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 6
- 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 6
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims description 6
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 6
- WJFKNYWRSNBZNX-UHFFFAOYSA-N 10H-phenothiazine Chemical compound C1=CC=C2NC3=CC=CC=C3SC2=C1 WJFKNYWRSNBZNX-UHFFFAOYSA-N 0.000 claims description 5
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 5
- SZXQTJUDPRGNJN-UHFFFAOYSA-N dipropylene glycol Chemical compound OCCCOCCCO SZXQTJUDPRGNJN-UHFFFAOYSA-N 0.000 claims description 5
- 239000001530 fumaric acid Substances 0.000 claims description 5
- 229950000688 phenothiazine Drugs 0.000 claims description 5
- 229920002503 polyoxyethylene-polyoxypropylene Polymers 0.000 claims description 5
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims description 5
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 claims description 4
- 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 4
- WFUGQJXVXHBTEM-UHFFFAOYSA-N 2-hydroperoxy-2-(2-hydroperoxybutan-2-ylperoxy)butane Chemical compound CCC(C)(OO)OOC(C)(CC)OO WFUGQJXVXHBTEM-UHFFFAOYSA-N 0.000 claims description 4
- QZPSOSOOLFHYRR-UHFFFAOYSA-N 3-hydroxypropyl prop-2-enoate Chemical compound OCCCOC(=O)C=C QZPSOSOOLFHYRR-UHFFFAOYSA-N 0.000 claims description 4
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 claims description 4
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 4
- WQAQPCDUOCURKW-UHFFFAOYSA-N butanethiol Chemical compound CCCCS WQAQPCDUOCURKW-UHFFFAOYSA-N 0.000 claims description 4
- 239000003112 inhibitor Substances 0.000 claims description 4
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims description 4
- 239000011976 maleic acid Substances 0.000 claims description 4
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 4
- MADOXCFISYCULS-UHFFFAOYSA-N octyl 2-sulfanylacetate Chemical compound CCCCCCCCOC(=O)CS MADOXCFISYCULS-UHFFFAOYSA-N 0.000 claims description 4
- 238000006116 polymerization reaction Methods 0.000 claims description 4
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Substances [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 claims description 4
- OWHSTLLOZWTNTQ-UHFFFAOYSA-N 2-ethylhexyl 2-sulfanylacetate Chemical compound CCCCC(CC)COC(=O)CS OWHSTLLOZWTNTQ-UHFFFAOYSA-N 0.000 claims description 3
- OMIGHNLMNHATMP-UHFFFAOYSA-N 2-hydroxyethyl prop-2-enoate Chemical compound OCCOC(=O)C=C OMIGHNLMNHATMP-UHFFFAOYSA-N 0.000 claims description 3
- GNSFRPWPOGYVLO-UHFFFAOYSA-N 3-hydroxypropyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCO GNSFRPWPOGYVLO-UHFFFAOYSA-N 0.000 claims description 3
- DXPPIEDUBFUSEZ-UHFFFAOYSA-N 6-methylheptyl prop-2-enoate Chemical compound CC(C)CCCCCOC(=O)C=C DXPPIEDUBFUSEZ-UHFFFAOYSA-N 0.000 claims description 3
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 claims description 3
- VTXVGVNLYGSIAR-UHFFFAOYSA-N decane-1-thiol Chemical compound CCCCCCCCCCS VTXVGVNLYGSIAR-UHFFFAOYSA-N 0.000 claims description 3
- WNAHIZMDSQCWRP-UHFFFAOYSA-N dodecane-1-thiol Chemical compound CCCCCCCCCCCCS WNAHIZMDSQCWRP-UHFFFAOYSA-N 0.000 claims description 3
- KZCOBXFFBQJQHH-UHFFFAOYSA-N octane-1-thiol Chemical compound CCCCCCCCS KZCOBXFFBQJQHH-UHFFFAOYSA-N 0.000 claims description 3
- SFHANYOFMGEJCT-UHFFFAOYSA-N octyl 2-sulfanylpropanoate Chemical compound CCCCCCCCOC(=O)C(C)S SFHANYOFMGEJCT-UHFFFAOYSA-N 0.000 claims description 3
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- DNIAPMSPPWPWGF-VKHMYHEASA-N (+)-propylene glycol Chemical compound C[C@H](O)CO DNIAPMSPPWPWGF-VKHMYHEASA-N 0.000 claims description 2
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 claims description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N 1,3-propanediol Substances OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 claims description 2
- ZJCZFAAXZODMQT-UHFFFAOYSA-N 2-methylpentadecane-2-thiol Chemical compound CCCCCCCCCCCCCC(C)(C)S ZJCZFAAXZODMQT-UHFFFAOYSA-N 0.000 claims description 2
- NQSLZEHVGKWKAY-UHFFFAOYSA-N 6-methylheptyl 2-methylprop-2-enoate Chemical compound CC(C)CCCCCOC(=O)C(C)=C NQSLZEHVGKWKAY-UHFFFAOYSA-N 0.000 claims description 2
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 2
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 claims description 2
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims description 2
- QJAOYSPHSNGHNC-UHFFFAOYSA-N octadecane-1-thiol Chemical compound CCCCCCCCCCCCCCCCCCS QJAOYSPHSNGHNC-UHFFFAOYSA-N 0.000 claims description 2
- 125000005489 p-toluenesulfonic acid group Chemical group 0.000 claims description 2
- 229920005862 polyol Polymers 0.000 claims description 2
- 150000003077 polyols Chemical class 0.000 claims description 2
- 229920000166 polytrimethylene carbonate Polymers 0.000 claims description 2
- 235000013772 propylene glycol Nutrition 0.000 claims description 2
- GJBRNHKUVLOCEB-UHFFFAOYSA-N tert-butyl benzenecarboperoxoate Chemical compound CC(C)(C)OOC(=O)C1=CC=CC=C1 GJBRNHKUVLOCEB-UHFFFAOYSA-N 0.000 claims description 2
- VBZBISQOWJYWCC-UHFFFAOYSA-N 2-(2-carboxypropan-2-yldiazenyl)-2-methylpropanoic acid Chemical compound OC(=O)C(C)(C)N=NC(C)(C)C(O)=O VBZBISQOWJYWCC-UHFFFAOYSA-N 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 125000000687 hydroquinonyl group Chemical group C1(O)=C(C=C(O)C=C1)* 0.000 claims 1
- LWNSNYBMYBWJDN-UHFFFAOYSA-N octyl 3-sulfanylpropanoate Chemical compound CCCCCCCCOC(=O)CCS LWNSNYBMYBWJDN-UHFFFAOYSA-N 0.000 claims 1
- 239000003638 chemical reducing agent Substances 0.000 abstract description 22
- 230000014759 maintenance of location Effects 0.000 abstract description 8
- 206010008428 Chemical poisoning Diseases 0.000 abstract 1
- 125000005396 acrylic acid ester group Chemical group 0.000 abstract 1
- 150000001735 carboxylic acids Chemical class 0.000 abstract 1
- 238000004321 preservation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 239000007787 solid Substances 0.000 description 10
- 239000004567 concrete Substances 0.000 description 9
- 239000007788 liquid Substances 0.000 description 9
- 239000004568 cement Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 7
- 239000004570 mortar (masonry) Substances 0.000 description 6
- CPJRRXSHAYUTGL-UHFFFAOYSA-N isopentenyl alcohol Chemical compound CC(=C)CCO CPJRRXSHAYUTGL-UHFFFAOYSA-N 0.000 description 4
- 150000003384 small molecules Chemical class 0.000 description 4
- 239000008030 superplasticizer Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000000463 material Substances 0.000 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 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 238000010532 solid phase synthesis reaction Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001694 spray drying Methods 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- ZOJURKXMRQJKNF-UHFFFAOYSA-N [Bi].C(CO)O Chemical compound [Bi].C(CO)O ZOJURKXMRQJKNF-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000004815 dispersion polymer Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004574 high-performance concrete Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- YKUKCVFREHLDGI-UHFFFAOYSA-N octan-3-yl 2-sulfanylpropanoate Chemical compound CCCCCC(CC)OC(=O)C(C)S YKUKCVFREHLDGI-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- -1 polyoxypropylene Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- ASUAYTHWZCLXAN-UHFFFAOYSA-N prenol Chemical compound CC(C)=CCO ASUAYTHWZCLXAN-UHFFFAOYSA-N 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
- 238000012546 transfer 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
- C08F2/00—Processes of polymerisation
- C08F2/02—Polymerisation in bulk
-
- 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
- C08F2/00—Processes of polymerisation
- C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
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)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
本发明的一种粉末状聚羧酸系保坍剂及其制备方法,制备方法包括以下步骤:将丙烯酸或甲基丙烯酸与多元醇在催化剂作用下制备一种酯类单体,然后与丙烯酸酯或甲基丙烯酸酯、不饱和羧酸和/或酸酐及聚醚单体,在复合引发剂和疏水性链转移剂作用下进行本体共聚,得到熔融态聚羧酸系保坍剂,最后通过保温管道送至冷冻粉碎机进行低温粉碎,即制得粉末状聚羧酸系保坍剂。本发明通过调整聚羧酸系减水剂的酸醚比、引入丙烯酸酯或甲基丙烯酸酯及自制酯类单体,并通过油溶性及水溶性复合引发剂的组合,制备了一种粉末状聚羧酸系保坍剂。本发明的保坍剂具有高坍落度保持性能,降低了制备成本,且制备过程安全环保、无溶剂毒害。A powdery polycarboxylate slump retaining agent of the present invention and a preparation method thereof, the preparation method comprising the following steps: preparing an ester monomer with acrylic acid or methacrylic acid and a polyhydric alcohol under the action of a catalyst, and then reacting with an acrylic acid ester Or methacrylate, unsaturated carboxylic acid and/or acid anhydride and polyether monomer, carry out bulk copolymerization under the action of composite initiator and hydrophobic chain transfer agent, obtain molten polycarboxylic acid series slump-retaining agent, and finally pass heat preservation The pipeline is sent to a frozen pulverizer for low-temperature pulverization to obtain a powdered polycarboxylate slump-retaining agent. The present invention prepares a powdery polycarboxylate water reducer by adjusting the acid-ether ratio, introducing acrylate or methacrylate and self-made ester monomers, and combining oil-soluble and water-soluble composite initiators. Polycarboxylate slump retaining agent. The slump-retaining agent of the invention has high slump retention performance, reduces the preparation cost, and the preparation process is safe and environment-friendly without solvent poisoning.
Description
技术领域technical field
本发明属于建筑材料中的混凝土外加剂技术领域,具体涉及一种粉末状聚羧酸系保坍剂及其制备方法。The invention belongs to the technical field of concrete admixtures in building materials, and in particular relates to a powdery polycarboxylate slump-retaining agent and a preparation method thereof.
背景技术Background technique
随着我国核电、水利、桥梁、隧道等大型基础设施的兴起,尤其是国家铁路客运专线网工程的大规模实施,对聚羧酸系减水剂的市场需求持续增长。与传统的高效减水剂相比,聚羧酸系减水剂以其高减水率、低坍落度损失、低碱含量等优良性能已成为混凝土高性能化的关键材料。With the rise of my country's nuclear power, water conservancy, bridges, tunnels and other large-scale infrastructure, especially the large-scale implementation of the national railway passenger dedicated line network project, the market demand for polycarboxylate water reducers continues to grow. Compared with traditional high-efficiency water reducers, polycarboxylate water reducers have become the key materials for high-performance concrete due to their excellent properties such as high water reducing rate, low slump loss, and low alkali content.
目前市场上的聚羧酸系减水剂多为10~50%的液体产品,由于其优越的性能,越来越多被用于各种重点工程中。但经常由于工程施工地点较远、施工现场场地有限,导致存储、运输成本不断的增加,所以发展高浓度或固体聚羧酸产品是降低运输成本和推广聚羧酸系减水剂广泛使用的重要条件。干粉砂浆的广泛推广应用,也对固体聚羧酸系减水剂的生产应用提出了迫切需求。目前市场上的粉体聚羧酸系减水剂多为通过喷雾干燥方法得到,但是将其稀释成液体,与同浓度的液体聚羧酸系减水剂相比性能有所下降,这主要是聚羧酸系减水剂受热后发生部分交联引起。如果想得到性能优异的聚羧酸系减水剂粉体产品,只能采用低温的方式,不破坏聚羧酸系减水剂结构的条件下操作。Most of the polycarboxylate water reducers on the market are 10-50% liquid products. Due to their superior performance, they are increasingly used in various key projects. However, often due to the remote construction site and limited construction site, storage and transportation costs continue to increase. Therefore, the development of high-concentration or solid polycarboxylate products is important to reduce transportation costs and promote the widespread use of polycarboxylate-based water reducers. condition. The wide popularization and application of dry powder mortar has also put forward an urgent demand for the production and application of solid polycarboxylate superplasticizer. At present, most of the powder polycarboxylate water-reducers on the market are obtained by spray drying, but when they are diluted into liquids, their performance decreases compared with the liquid polycarboxylate water-reducers of the same concentration, which is mainly because The polycarboxylate water reducer is partially cross-linked after being heated. If you want to obtain polycarboxylate superplasticizer powder products with excellent performance, you can only operate at low temperature without destroying the structure of polycarboxylate superplasticizer.
CN102372458A报道了一种固体聚羧酸系减水剂的制备方法,由不饱和酸和其他不饱和单体在有机溶剂中进行共聚,经分离沉淀和低温干燥后制备得到。该固体减水剂在溶于水溶剂中,与市售同样浓度的液体聚羧酸系减水剂产品相比,综合性能没有差异。但该专利需要用到有机溶剂如醇、芳香烃、脂肪烃、酯等,得到聚合产物之后还需要干燥分离溶剂,生产过程不够绿色化。CN102372458A reports a method for preparing a solid polycarboxylic acid-based water reducer, which is prepared by copolymerizing unsaturated acid and other unsaturated monomers in an organic solvent, followed by separation, precipitation and low-temperature drying. When the solid water reducer is dissolved in a water solvent, there is no difference in overall performance compared with commercially available liquid polycarboxylate water reducer products of the same concentration. However, this patent requires the use of organic solvents such as alcohols, aromatic hydrocarbons, aliphatic hydrocarbons, esters, etc. After obtaining the polymerized product, it is necessary to dry and separate the solvent, and the production process is not green enough.
CN103554382A报道了一种固相合成聚羧酸系减水剂的方法,将聚醚单体、引发剂和少量水加入到球磨机或胶体磨中,开动机器混合10分钟,再分若干次将小分子单体、还原剂、链转移剂和小分子单体质量10%的水组成的混合物等份加入球磨机或胶体磨中,全部加完后,再继续反应1h,就可以得到固体或膏状聚羧酸系减水剂。CN103554382A reports a method for solid-phase synthesis of polycarboxylic acid-based water reducers. Add polyether monomers, initiators and a small amount of water to a ball mill or colloid mill, start the machine and mix for 10 minutes, and then divide the small molecule several times. Add the mixture of monomer, reducing agent, chain transfer agent and water with 10% mass of small molecule monomer into the ball mill or colloid mill in equal parts. Acid-based water reducer.
CN103755885A提出了一种微波辅助固相合成聚羧酸系减水剂的方法,将聚醚单体、引发剂、小分子单体、还原剂、链转移剂和小分子单体质量50%的水组成的糊状混合物置于功率可调的微波炉中,反应一定时间,得到固体或膏状聚羧酸系减水剂。上述专利中的方法不适宜大规模工业化生产。CN103755885A proposes a method for microwave-assisted solid-phase synthesis of polycarboxylic acid-based water reducers, in which polyether monomers, initiators, small molecule monomers, reducing agents, chain transfer agents and small molecule monomers are mixed with 50% water The formed pasty mixture is placed in a microwave oven with adjustable power, and reacted for a certain period of time to obtain a solid or pasty polycarboxylate water reducer. The method in the above-mentioned patent is not suitable for large-scale industrial production.
CN102993387B报道了一种通过一步直接合成纯固体聚羧酸系减水剂的制备方法,将不饱和聚氧乙烯醚加热至50~70℃熔化,依次向反应器中加入分子量调节剂、(甲基)丙烯酸或其与不饱和羧酸的混合物单体、引发剂,并且每次加料间隔搅拌时间5~20分钟,继续升温至75~95℃下进行本体聚合反应1.5~8h,冷却至室温即得到纯固体聚羧酸系减水剂。上述两种方法存在温度偏高或工艺复杂的缺陷。CN102993387B reports a preparation method for directly synthesizing pure solid polycarboxylate water reducer in one step, heating unsaturated polyoxyethylene ether to 50-70°C to melt, adding molecular weight regulator, (methyl ) acrylic acid or its mixture with unsaturated carboxylic acid monomer and initiator, and the stirring time between each addition is 5-20 minutes, continue to heat up to 75-95 ° C for bulk polymerization for 1.5-8 hours, and cool to room temperature to obtain Pure solid polycarboxylate superplasticizer. The above two methods have the defects of high temperature or complex process.
发明内容Contents of the invention
针对上述问题,本发明公开一种粉末状聚羧酸系保坍剂及其制备方法,通过共聚物分子中羧基密度、侧链长度的调整及缓释性的酯基等功能性基团的引入,制备具有高坍落度保持性能的混凝土保坍剂,与聚羧酸系减水剂具有良好的相容性及优异的坍落度保持能力。In view of the above problems, the present invention discloses a powdery polycarboxylate slump-retaining agent and its preparation method, through the adjustment of the carboxyl group density in the copolymer molecule, the length of the side chain and the introduction of functional groups such as slow-release ester groups , to prepare a concrete slump retaining agent with high slump retention performance, which has good compatibility with polycarboxylate water reducer and excellent slump retention ability.
本发明涉及一种粉末状聚羧酸系保坍剂的制备方法,其特征在于按重量百分比计,包括下述原料组成:The present invention relates to a kind of preparation method of powdery polycarboxylic acid series slump-retaining agent, it is characterized in that by weight percentage, comprises following raw material composition:
所述多元醇为乙二醇、二乙二醇、1,2-丙二醇、1,3-丙二醇、一缩二丙二醇中的一种。The polyhydric alcohol is one of ethylene glycol, diethylene glycol, 1,2-propanediol, 1,3-propanediol and dipropylene glycol.
所述催化剂为对甲苯磺酸或氨基磺酸,所述阻聚剂为对苯二酚、吩噻嗪、二苯胺中的一种。The catalyst is p-toluenesulfonic acid or sulfamic acid, and the polymerization inhibitor is one of hydroquinone, phenothiazine and diphenylamine.
所述聚醚单体为分子量600~4000的甲基烯丙醇聚氧乙烯醚、甲基烯丙醇聚氧乙烯聚氧丙烯醚、异戊烯醇聚氧乙烯醚、异戊烯醇聚氧乙烯聚氧丙烯醚中的一种。The polyether monomer is methallyl alcohol polyoxyethylene ether, methallyl alcohol polyoxyethylene polyoxypropylene ether, prenyl alcohol polyoxyethylene ether, isopentenyl alcohol polyoxyethylene ether, and isopentenyl alcohol polyoxyethylene ether with a molecular weight of 600-4000. One of ethylene polyoxypropylene ethers.
所述不饱和羧酸为酸酐为丙烯酸、甲基丙烯酸、富马酸、马来酸、马来酸酐中的至少一种,或所述不饱和羧酸为不饱和羧酸与酸酐为丙烯酸、甲基丙烯酸、富马酸、马来酸、马来酸酐中的至少一种的混合。The unsaturated carboxylic acid is that the acid anhydride is at least one of acrylic acid, methacrylic acid, fumaric acid, maleic acid, maleic anhydride, or the unsaturated carboxylic acid is an unsaturated carboxylic acid and the acid anhydride is acrylic acid, methyl A mixture of at least one of acrylic acid, fumaric acid, maleic acid, and maleic anhydride.
所述丙烯酸酯包括丙烯酸甲酯、丙烯酸乙酯、丙烯酸异辛酯、丙烯酸羟乙酯、丙烯酸羟丙酯中的一种;所述甲基丙烯酸酯包括甲基丙烯酸甲酯、甲基丙烯酸乙酯、甲基丙烯酸异辛酯、甲基丙烯酸羟乙酯、甲基丙烯酸羟丙酯中的一种。Described acrylate comprises one in methyl acrylate, ethyl acrylate, isooctyl acrylate, hydroxyethyl acrylate, hydroxypropyl acrylate; Described methacrylate comprises methyl methacrylate, ethyl methacrylate , one of isooctyl methacrylate, hydroxyethyl methacrylate, and hydroxypropyl methacrylate.
所述油溶性引发剂为偶氮二异丁腈、偶氮二异庚腈、偶氮二异丁酸二甲酯、过氧化苯甲酰、过氧化苯甲酰叔丁酯、过氧化甲乙酮中的一种,所述水溶性引发剂为过硫酸铵、过硫酸钠及过硫酸钾中的一种。The oil-soluble initiator is azobisisobutyronitrile, azobisisoheptanonitrile, dimethyl azobisisobutyrate, benzoyl peroxide, benzoyl tert-butyl peroxide, methyl ethyl ketone peroxide A kind of, described water-soluble initiator is a kind of in ammonium persulfate, sodium persulfate and potassium persulfate.
所述链转移剂为疏水性链转移剂,包括丁硫醇、辛硫醇、癸硫醇、月桂基硫醇、十六烷基硫醇、十八烷基硫醇、2-巯基丙酸辛酯、3-巯基丙酸辛酯、硫代羟乙酸辛酯、巯基乙酸-2-乙基己酯,可以单独使用或者组合使用两种或以上。The chain transfer agent is a hydrophobic chain transfer agent, including butyl mercaptan, octyl mercaptan, decyl mercaptan, lauryl mercaptan, hexadecyl mercaptan, octadecyl mercaptan, octyl 2-mercaptopropionate , 3-octyl mercaptopropionate, octyl thioglycolate, and 2-ethylhexyl thioglycolate can be used alone or in combination of two or more.
上述的粉末状聚羧酸系保坍剂的制备方法,包括以下步骤:The preparation method of above-mentioned powdery polycarboxylate series slump-retaining agent, comprises the following steps:
将丙烯酸或甲基丙烯酸与多元醇在催化剂作用下制备一种酯类单体,然后与丙烯酸酯或甲基丙烯酸酯、不饱和羧酸和/或酸酐、和聚醚单体,在复合引发剂和疏水性链转移剂作用下进行本体共聚,得到熔融态聚羧酸系保坍剂,最后通过保温管道送至冷冻粉碎机进行低温粉碎,即制得粉末状聚羧酸系保坍剂。本发明通过调整聚羧酸系减水剂的酸醚比、引入丙烯酸酯或甲基丙烯酸酯及自制酯类单体,并通过油溶性及水溶性复合引发剂的组合,制备了一种粉末状聚羧酸系保坍剂。Acrylic acid or methacrylic acid and polyhydric alcohol are prepared as an ester monomer under the action of a catalyst, and then mixed with acrylate or methacrylate, unsaturated carboxylic acid and/or acid anhydride, and polyether monomer, in the composite initiator Bulk copolymerization under the action of a hydrophobic chain transfer agent to obtain a molten polycarboxylate slump retaining agent, and finally sent to a freezing pulverizer through an insulated pipeline for low-temperature pulverization to obtain a powdered polycarboxylate slump retainer. The present invention prepares a powdery polycarboxylate water reducer by adjusting the acid-ether ratio, introducing acrylate or methacrylate and self-made ester monomers, and combining oil-soluble and water-soluble composite initiators. Polycarboxylate slump retaining agent.
更具体的,制备方法的步骤为:(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中,加入计量的丙烯酸或甲基丙烯酸、多元醇、催化剂及阻聚剂,在搅拌下升温至90~120℃,搅拌回流2~7h,用分水器分出水层并降温至60~70℃;More specifically, the steps of the preparation method are: (1) Preparation of ester monomers: add metered acrylic acid or methyl Acrylic acid, polyol, catalyst and polymerization inhibitor are heated to 90-120°C under stirring, stirred and refluxed for 2-7 hours, and the water layer is separated with a water separator and cooled to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:反应釜中加入计量的聚醚单体,搅拌熔解,再加入油溶性引发剂搅拌溶解;接着将水溶性引发剂、链转移剂及丙烯酸配成混合溶液,并在2~4h内用恒流泵滴完;滴完后继续保温2~4h,加入一定量粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid-based slump-retaining agent: add metered polyether monomer into the reactor, stir and melt, then add oil-soluble initiator and stir to dissolve; then add water-soluble initiator, chain transfer agent and acrylic acid Make a mixed solution, and use a constant flow pump to drip it within 2 to 4 hours; continue to keep warm for 2 to 4 hours after dropping, add a certain amount of powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:熔融产物通过保温管道送至冷冻粉碎机,在-20~-40℃下进行低温粉碎,即制得细度为100~200目的粉末状聚羧酸系保坍剂。(3) Preparation of powdered polycarboxylate-based slump-retaining agent: the melted product is sent to a frozen pulverizer through an insulated pipeline, and is ground at -20 to -40°C at a low temperature to obtain a powder with a fineness of 100 to 200 meshes. Polycarboxylate slump retaining agent.
所述引发剂为同时包含油溶性及水溶性引发剂的复合引发剂,其加入方式为油溶性引发剂作为底料一次性投入反应釜中,水溶性引发剂溶于不饱和羧酸缓慢滴加到反应釜中。The initiator is a composite initiator containing both oil-soluble and water-soluble initiators, and its addition method is that the oil-soluble initiator is put into the reaction kettle at one time as a base material, and the water-soluble initiator is dissolved in unsaturated carboxylic acid and slowly added dropwise into the reactor.
本发明方法与现有技术相比具有以下有益效果:Compared with the prior art, the inventive method has the following beneficial effects:
(1)采用本发明制备的粉末状聚羧酸系保坍剂,可以避免喷雾干燥处理导致的化学副反应或挂壁灼烧等问题,丰富制备聚羧酸系保坍剂的方法。(1) The powdery polycarboxylate slump-retaining agent prepared by the present invention can avoid problems such as chemical side reactions or wall-hanging burning caused by spray drying, and enrich the method for preparing polycarboxylate-based slump-retaining agents.
(2)制备过程安全环保、无溶剂毒害、清洁无污染,所用反应原料简单常见,合成过程无需氮气保护,大大降低了生产成本。(2) The preparation process is safe, environmentally friendly, solvent-free, clean and pollution-free, the reaction raw materials used are simple and common, and the synthesis process does not require nitrogen protection, which greatly reduces the production cost.
(3)本发明根据分子设计理论,在聚合物中引入的酯类单体及丙烯酸酯或甲基丙烯酸酯部分取代丙烯酸或甲基丙烯酸,减小了分子主链中的羧基密度,调整吸附平衡,实现了聚合物分散性能和保坍性能的调控,且由于各单体水解的速率不同,保坍效果持续时间可以根据实际情况进行调整,适应性更好。(3) According to the theory of molecular design, the present invention partially replaces acrylic acid or methacrylic acid with ester monomers and acrylate or methacrylate introduced in the polymer, which reduces the carboxyl density in the molecular main chain and adjusts the adsorption balance , to achieve the control of polymer dispersion performance and slump retention performance, and because the hydrolysis rate of each monomer is different, the duration of the slump retention effect can be adjusted according to the actual situation, and the adaptability is better.
(4)本发明制备所得保坍剂在较低掺量下仍能表现出较好的流动性保持能力,并且对不同品种的水泥表现出很强的适应性。此外,保坍剂产品状态稳定,低温下存放不结晶,且低温储存后性能不受影响,有利于工业化推广应用,具有良好的经济效益和社会效益。(4) The slump-retaining agent prepared by the present invention can still show better fluidity retention ability at a lower dosage, and shows strong adaptability to different types of cement. In addition, the slump-retaining agent product is stable, does not crystallize when stored at low temperature, and its performance is not affected after low-temperature storage, which is conducive to industrialization and application, and has good economic and social benefits.
(5)本发明的粉末状聚羧酸系保坍剂,可以广泛应于用商品砂浆、灌缝砂浆及各种特种砂浆,弥补了以往干粉砂浆中只能使用缓凝剂保塑的不足或者由于使用液体保坍剂带来的应用不便,可有效推动干粉砂浆技术的发展。(5) The powdery polycarboxylate series slump-retaining agent of the present invention can be widely used in commercial mortar, grouting mortar and various special mortars, making up for the deficiency that only retarders can be used in dry powder mortar in the past or plastic-retaining agents. Due to the inconvenience of application caused by the use of liquid slump retaining agent, it can effectively promote the development of dry powder mortar technology.
具体实施方式detailed description
以下用具体实施例来详细说明本发明的实施方式,借此对本发明如何应用技术手段来解决技术问题,并达成技术效果的实现过程能充分理解并据以实施。The implementation of the present invention will be described in detail below with specific examples, so as to fully understand and implement the process of how to apply technical means to solve technical problems and achieve technical effects in the present invention.
本发明实施例通过调整聚羧酸系减水剂的酸醚比及引入自制酯类单体,并通过油溶性及水溶性复合引发剂的组合,在熔融状态下制备了一种固体聚羧酸系保坍剂。由于不存在大量的水,存储、运输更为方便,而且大大降低了运输成本。In the embodiment of the present invention, a solid polycarboxylic acid is prepared in a molten state by adjusting the acid-ether ratio of the polycarboxylic acid-based water reducer, introducing self-made ester monomers, and combining oil-soluble and water-soluble composite initiators. Department of anti-slump agent. Since there is no large amount of water, storage and transportation are more convenient, and transportation costs are greatly reduced.
实施例1:Example 1:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入312.8kg甲基丙烯酸、94.0kg乙二醇、8.1kg氨基磺酸及2.0kg对苯二酚,在搅拌下升温至110~120℃,搅拌回流3~3.5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 312.8kg methacrylic acid, 94.0kg ethylene glycol, 8.1kg sulfamic acid to the reaction kettle equipped with thermometer, stirring paddle, constant flow pump, condenser and water separator and 2.0kg of hydroquinone, heat up to 110-120°C under stirring, stir and reflux for 3-3.5 hours, separate the water layer with a water separator and lower the temperature to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入4168kg异戊烯醇聚氧乙烯醚(分子量2400),搅拌熔解,再加入29.2kg过氧化苯甲酰搅拌溶解;接着将19.5kg过硫酸钠、38.9kg硫代羟乙酸辛酯、86.8kg丙烯酸乙酯及187.6kg丙烯酸配成混合溶液,并在3.5~4h内用恒流泵滴完;滴完后继续保温2~2.5h,加入53.1kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 4168kg isopentenol polyoxyethylene ether (molecular weight 2400), stir and melt, then add 29.2kg benzoyl peroxide and stir to dissolve; then 19.5kg over Sodium sulfate, 38.9kg of octyl thioglycolate, 86.8kg of ethyl acrylate and 187.6kg of acrylic acid were mixed into a mixed solution, which was dripped with a constant-flow pump within 3.5-4 hours; Stir 53.1kg powder alkali evenly;
(3)粉末状聚羧酸系保坍剂的制备:熔融产物通过保温管道送至冷冻粉碎机低温粉碎,即制得白色粉末状聚羧酸系保坍剂。(3) Preparation of powdered polycarboxylate-based slump-retaining agent: the melted product is sent to a freezer pulverizer for low-temperature pulverization through an insulated pipeline to obtain a white powder-like polycarboxylate-based slump-retaining agent.
实施例2:Example 2:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入417.8kg甲基丙烯酸、125.5kg乙二醇、10.9kg氨基磺酸及2.7kg对苯二酚,在搅拌下升温至110~120℃,搅拌回流3~3.5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 417.8kg methacrylic acid, 125.5kg ethylene glycol, 10.9kg sulfamic acid to the reaction kettle equipped with thermometer, stirring paddle, constant flow pump, condenser and water separator and 2.7kg of hydroquinone, heat up to 110-120°C under stirring, stir and reflux for 3-3.5 hours, separate the water layer with a water separator and cool down to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入3712kg异戊烯醇聚氧乙烯聚氧丙烯醚(分子量1600),搅拌熔解,再加入29.0kg偶氮二异庚腈搅拌溶解;接着将19.2kg过硫酸铵、33.9kg丁硫醇、269.1kg丙烯酸羟乙酯及299.2kg甲基丙烯酸配成混合溶液,并在2.5~3h内用恒流泵滴完;滴完后继续保温4h,加入80.9kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 3712kg isopentenol polyoxyethylene polyoxypropylene ether (molecular weight 1600), stir and melt, then add 29.0kg azobisisoheptanonitrile and stir to dissolve; then Mix 19.2kg of ammonium persulfate, 33.9kg of butanethiol, 269.1kg of hydroxyethyl acrylate and 299.2kg of methacrylic acid into a mixed solution, and drop it with a constant-current pump within 2.5 to 3 hours; continue to keep warm for 4 hours after dropping, Add 80.9kg powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例3:Example 3:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入707.0kg甲基丙烯酸、212.4kg乙二醇、18.4kg氨基磺酸及4.6kg对苯二酚,在搅拌下升温至100~110℃,搅拌回流4~5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 707.0kg methacrylic acid, 212.4kg ethylene glycol, 18.4kg sulfamic acid to the reaction kettle equipped with thermometer, stirring paddle, constant flow pump, condenser and water separator and 4.6kg of hydroquinone, heated up to 100-110°C under stirring, stirred and refluxed for 4-5 hours, separated the water layer with a water separator and lowered the temperature to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入3140kg异戊烯醇聚氧乙烯醚(分子量1200),搅拌熔解,再加入384.8kg马来酸酐及33.5kg过氧化苯甲酰搅拌溶解;接着将14.4kg过硫酸钠、38.5kg3-巯基丙酸辛酯及340.3kg甲基丙烯酸羟乙酯配成混合溶液,并在3h内用恒流泵滴完;滴完后继续保温3.5~4h,加入106.1kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylate slump-retaining agent: add 3140kg isopentenol polyoxyethylene ether (molecular weight 1200), stir and melt, then add 384.8kg maleic anhydride and 33.5kg benzoyl peroxide and stir to dissolve ; Then 14.4kg of sodium persulfate, 38.5kg of 3-mercaptopropionate octyl and 340.3kg of hydroxyethyl methacrylate are formulated into a mixed solution, and are dripped with a constant flow pump within 3 hours; Add 106.1kg powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例4:Example 4:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入220.6kg丙烯酸、146.6kg一缩二丙二醇、5.5kg氨基磺酸及1.9kg吩噻嗪,在搅拌下升温至110~120℃,搅拌回流3~3.5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 220.6kg acrylic acid, 146.6kg dipropylene glycol, 5.5kg sulfamic acid and 1.9kg of phenothiazine, heat up to 110-120°C under stirring, stir and reflux for 3-3.5 hours, separate the water layer with a water separator and cool down to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入4280kg异戊烯醇聚氧乙烯醚(分子量4000),搅拌熔解,再加入34.1kg偶氮二异丁酸二甲酯搅拌溶解;接着将14.7kg过硫酸铵、29.3kg癸硫醇、69.6kg丙烯酸羟丙酯及154.1kg丙烯酸配成混合溶液,并在2~2.5h内用恒流泵滴完;滴完后继续保温3.5~4h,加入43.6kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 4280kg isopentenol polyoxyethylene ether (molecular weight 4000), stir and melt, then add 34.1kg dimethyl azobisisobutyrate and stir to dissolve; then Mix 14.7kg of ammonium persulfate, 29.3kg of decyl mercaptan, 69.6kg of hydroxypropyl acrylate and 154.1kg of acrylic acid to make a mixed solution, and use a constant flow pump to drop it within 2 to 2.5 hours; after the drop, continue to keep warm for 3.5 to 4 hours , add 43.6kg powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例5:Example 5:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入382.1kg丙烯酸、254.0kg一缩二丙二醇、9.5kg氨基磺酸及3.2kg吩噻嗪,在搅拌下升温至100~110℃,搅拌回流4~5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 382.1kg acrylic acid, 254.0kg dipropylene glycol, 9.5kg sulfamic acid and 3.2kg of phenothiazine, heat up to 100-110°C under stirring, stir and reflux for 4-5 hours, separate the water layer with a water separator and cool down to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入3708kg异戊烯醇聚氧乙烯醚(分子量2000),搅拌熔解,再加入24.1kg过氧化甲乙酮搅拌溶解;接着将24.1kg过硫酸钾、33.7kg硫代羟乙酸辛酯、159.4kg丙烯酸甲酯及318.8kg甲基丙烯酸配成混合溶液,并在3h内用恒流泵滴完;滴完后继续保温4h,加入83.1kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 3708kg isopentenol polyoxyethylene ether (molecular weight 2000), stir and melt, then add 24.1kg methyl ethyl ketone peroxide and stir to dissolve; then 24.1kg potassium persulfate , 33.7kg octyl thioglycolate, 159.4kg methyl acrylate and 318.8kg methacrylic acid to make a mixed solution, and drop it with a constant flow pump within 3 hours; after dropping, continue to keep warm for 4 hours, add 83.1kg powder alkali and stir Uniform;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例6:Embodiment 6:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入693.2kg丙烯酸、460.7kg一缩二丙二醇、17.3kg氨基磺酸及5.8kg吩噻嗪,在搅拌下升温至110~120℃,搅拌回流3~3.5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 693.2kg acrylic acid, 460.7kg dipropylene glycol, 17.3kg sulfamic acid and 5.8kg of phenothiazine, heat up to 110-120°C under stirring, stir and reflux for 3-3.5 hours, separate the water layer with a water separator and cool down to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入2690kg异戊烯醇聚氧乙烯醚(分子量800),搅拌熔解,再加入23.9kg过氧化甲乙酮搅拌溶解;接着将23.9kg过硫酸钾、28.6kg辛硫醇、437.2kg丙烯酸羟丙酯及484.3kg丙烯酸配成混合溶液,并在2~2.5h内用恒流泵滴完;滴完后继续保温3~3.5h,加入135.1kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylate slump-retaining agent: add 2690kg isopentenol polyoxyethylene ether (molecular weight 800), stir and melt, then add 23.9kg methyl ethyl ketone peroxide and stir to dissolve; then 23.9kg potassium persulfate , 28.6kg octyl mercaptan, 437.2kg hydroxypropyl acrylate and 484.3kg acrylic acid to make a mixed solution, and use a constant flow pump to drip it within 2~2.5h; Stir the alkali evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例7:Embodiment 7:
(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入307.7kg丙烯酸、141.6kg二乙二醇、8.1kg对甲苯磺酸及2.2kg二苯胺,在搅拌下升温至100~110℃,搅拌回流4~4.5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: add 307.7kg of acrylic acid, 141.6kg of diethylene glycol, and 8.1kg of p-toluenesulfonic acid into a reaction kettle equipped with a thermometer, a stirring blade, a constant flow pump, a condenser and a water separator and 2.2kg of diphenylamine, heated to 100-110°C under stirring, stirred and refluxed for 4-4.5 hours, separated the water layer with a water separator and lowered the temperature to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入3804kg甲基烯丙醇聚氧乙烯醚(分子量2400),搅拌熔解,再加入459.6kg富马酸及33.8kg过氧化苯甲酰搅拌溶解;接着将14.4kg过硫酸钾、38.7kg巯基乙酸-2-乙基己酯及103.0kg甲基丙烯酸羟乙酯配成混合溶液,并在2~2.5h内用恒流泵滴完;滴完后继续保温3.5~4h,加入86.9kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 3804kg methallyl alcohol polyoxyethylene ether (molecular weight 2400), stir and melt, then add 459.6kg fumaric acid and 33.8kg benzoyl peroxide and stir Dissolve; then mix 14.4kg of potassium persulfate, 38.7kg of 2-ethylhexyl mercaptoacetate and 103.0kg of hydroxyethyl methacrylate into a mixed solution, and drop it with a constant flow pump within 2 to 2.5 hours; After that, continue to keep warm for 3.5-4 hours, add 86.9kg powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例8:Embodiment 8:
(1)酯类单体的制备:(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入255.8kg丙烯酸、117.8kg二乙二醇、6.7kg对甲苯磺酸及1.9kg二苯胺,在搅拌下升温至110~120℃,搅拌回流3~3.5h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: (1) Preparation of ester monomers: add 255.8kg acrylic acid, 117.8kg bismuth Ethylene glycol, 6.7kg of p-toluenesulfonic acid and 1.9kg of diphenylamine are heated to 110-120°C under stirring, stirred and refluxed for 3-3.5 hours, and the water layer is separated with a water separator and cooled to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入3953kg异戊烯醇聚氧乙烯醚(分子量3000),搅拌熔解,再加入29.1kg过氧化苯甲酰叔丁酯搅拌溶解;接着将19.4kg过硫酸钠、24.2kg 2-巯基丙酸辛酯、242.5kg丙烯酸异辛酯及283.3kg甲基丙烯酸配成混合溶液,并在2~2.5h内用恒流泵滴完;滴完后继续保温3.5~4h,加入66.3kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 3953kg isopentenol polyoxyethylene ether (molecular weight 3000), stir and melt, then add 29.1kg benzoyl peroxide and stir to dissolve; 19.4kg of sodium persulfate, 24.2kg of octyl 2-mercaptopropionate, 242.5kg of isooctyl acrylate and 283.3kg of methacrylic acid were prepared as a mixed solution, and the solution was dripped with a constant flow pump within 2 to 2.5 hours; Keep warm for 3.5-4 hours, add 66.3kg powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
实施例9:Embodiment 9:
(1)酯类单体的制备:(1)酯类单体的制备:向装有温度计、搅拌浆、恒流泵、冷凝器及分水器的反应釜中加入446.8kg丙烯酸、205.5kg二乙二醇、11.8kg对甲苯磺酸及3.2kg二苯胺,在搅拌下升温至90~95℃,搅拌回流5.5~6h,用分水器分出水层并降温至60~70℃;(1) Preparation of ester monomers: (1) Preparation of ester monomers: add 446.8kg acrylic acid, 205.5kg dihydrogen to the reaction kettle equipped with thermometer, stirring paddle, constant flow pump, condenser and water separator Ethylene glycol, 11.8kg of p-toluenesulfonic acid and 3.2kg of diphenylamine are heated to 90-95°C under stirring, stirred and refluxed for 5.5-6 hours, and the water layer is separated with a water separator and cooled to 60-70°C;
(2)熔融态聚羧酸系保坍剂的制备:加入3680kg甲基烯丙醇聚氧乙烯聚氧丙烯醚(分子量2400),搅拌熔解,再加入29.2kg偶氮二异丁腈搅拌溶解;接着将19.3kg过硫酸铵、29.2kg月桂基硫醇、220.9kg甲基丙烯酸羟丙酯及276.1kg丙烯酸配成混合溶液,并在2h~2.5h内用恒流泵滴完;滴完后继续保温3~3.5h,加入78.0kg粉碱搅拌均匀;(2) Preparation of molten polycarboxylic acid series slump-retaining agent: add 3680kg methallyl alcohol polyoxyethylene polyoxypropylene ether (molecular weight 2400), stir and melt, then add 29.2kg azobisisobutyronitrile and stir to dissolve; Then, 19.3kg of ammonium persulfate, 29.2kg of lauryl mercaptan, 220.9kg of hydroxypropyl methacrylate and 276.1kg of acrylic acid were formulated into a mixed solution, which was dripped with a constant flow pump within 2h to 2.5h; after dripping, continue Keep warm for 3-3.5 hours, add 78.0kg powder alkali and stir evenly;
(3)粉末状聚羧酸系保坍剂的制备:同实施例1。(3) Preparation of powdery polycarboxylate slump retaining agent: same as Example 1.
应用实施例1:Application Example 1:
水泥净浆流动度参照国家标准GB/T 8077-2012《混凝土外加剂匀质性试验方法》,三种水泥分别是基准水泥、中国水泥厂有限公司的海螺P·O42.5级及南京-小野田水泥有限公司的金宁羊P·II52.5级;对比的液体聚羧酸系保坍剂选用南京瑞迪高新技术有限公司的TX-209和江苏某厂的ST-412,保坍剂的掺量为0.2%(以折固后水泥的重量为基准计),试验结果见表1。The fluidity of cement slurry refers to the national standard GB/T 8077-2012 "Concrete Admixture Homogeneity Test Method". Jinning sheep P·II52.5 grade of Cement Co., Ltd.; the comparative liquid polycarboxylate slump retaining agent is TX-209 from Nanjing Ruidi High-tech Co., Ltd. and ST-412 from a factory in Jiangsu. The amount is 0.2% (based on the weight of cement after folding), and the test results are shown in Table 1.
表1不同保坍剂的净浆流动度及损失对比Table 1 Comparison of net slurry fluidity and loss of different slump-retaining agents
由表1结果可见,本发明的固体聚羧酸系保坍剂在不同水泥中的初始水泥净浆流动度方面表现差异较大,但均具有良好的流动度保持能力,普遍具有经时增长,与对比的液体聚羧酸系保坍剂TX-209性能相近,优于市售的液体聚羧酸系保坍剂ST-412。As can be seen from the results in Table 1, the solid polycarboxylate-based slump-retaining agent of the present invention has a large difference in the fluidity of the initial cement paste in different cements, but all have good fluidity retention capabilities, and generally have a time-dependent growth. The performance is similar to that of the comparative liquid polycarboxylate slump retaining agent TX-209, and better than the commercially available liquid polycarboxylate slump retainer ST-412.
应用实施例2:Application Example 2:
参照国家标准GB 8076-2008《混凝土外加剂》相关规定执行。试验水泥采用基准水泥,外加剂均为固掺0.2%,混凝土配合比见表2,试验结果见下表3。Refer to the relevant provisions of the national standard GB 8076-2008 "Concrete Admixtures". The benchmark cement was used for the test cement, and the admixtures were solidly mixed with 0.2%. The concrete mix ratio is shown in Table 2, and the test results are shown in Table 3 below.
表2混凝土配合比(kg/m3)Table 2 Concrete mix ratio (kg/m 3 )
表3不同聚羧酸系保坍剂的混凝土性能对比Table 3 Concrete performance comparison of different polycarboxylate slump-retaining agents
结果表明,本发明的固体聚羧酸系保坍剂均有较好的混凝土坍落度保持能力,2h后混凝土仍具有良好的流动性,与对比的液体聚羧酸系保坍剂TX-209性能接近,优于市售的液体聚羧酸系保坍剂ST-412。The results show that the solid polycarboxylate slump retaining agent of the present invention has good concrete slump retention ability, and the concrete still has good fluidity after 2 hours, compared with the liquid polycarboxylate slump retaining agent TX-209 of contrast The performance is close to that of the commercially available liquid polycarboxylate slump retaining agent ST-412.
虽然本发明通过实施例进行了描述,但实施例并非用来限定本发明。本领域技术人员可在本发明的精神的范围内,做出各种变形和改进,例如成分比例或时间范围的调整,这种调整后的效果是可预测的,所以其同样在本发明的保护范围之内。因此本发明的保护范围应当以本申请的权利要求相同或等同的技术特征所界定的保护范围为准。While the present invention has been described by way of examples, the examples are not intended to limit the invention. Those skilled in the art can make various modifications and improvements within the scope of the spirit of the present invention, such as the adjustment of component ratios or time ranges. The effect after this adjustment is predictable, so it is also within the scope of the protection of the present invention. within range. Therefore, the protection scope of the present invention should be determined by the protection scope defined by the same or equivalent technical features of the claims of this application.
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