CN101993210B - Prenyl polyether polycarboxylate water reducing agent and synthesis method thereof - Google Patents
Prenyl polyether polycarboxylate water reducing agent and synthesis method thereof Download PDFInfo
- Publication number
- CN101993210B CN101993210B CN 201010119880 CN201010119880A CN101993210B CN 101993210 B CN101993210 B CN 101993210B CN 201010119880 CN201010119880 CN 201010119880 CN 201010119880 A CN201010119880 A CN 201010119880A CN 101993210 B CN101993210 B CN 101993210B
- Authority
- CN
- China
- Prior art keywords
- isoprenyl
- macromonomer
- reducing agent
- small monomer
- water
- 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.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 68
- 239000003638 chemical reducing agent Substances 0.000 title claims abstract description 37
- 229920005646 polycarboxylate Polymers 0.000 title claims abstract description 22
- 239000004721 Polyphenylene oxide Substances 0.000 title claims abstract description 16
- 229920000570 polyether Polymers 0.000 title claims abstract description 16
- 238000001308 synthesis method Methods 0.000 title abstract description 4
- 125000001844 prenyl group Chemical group [H]C([*])([H])C([H])=C(C([H])([H])[H])C([H])([H])[H] 0.000 title 1
- -1 isoprenyl Chemical group 0.000 claims abstract description 24
- 239000000178 monomer Substances 0.000 claims abstract description 20
- 229920000056 polyoxyethylene ether Polymers 0.000 claims abstract description 13
- 229940051841 polyoxyethylene ether Drugs 0.000 claims abstract description 12
- 239000012986 chain transfer agent Substances 0.000 claims abstract description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 48
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims description 38
- 239000008367 deionised water Substances 0.000 claims description 31
- 229910021641 deionized water Inorganic materials 0.000 claims description 31
- CWERGRDVMFNCDR-UHFFFAOYSA-N thioglycolic acid Chemical compound OC(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-N 0.000 claims description 26
- ZZZCUOFIHGPKAK-UHFFFAOYSA-N D-erythro-ascorbic acid Natural products OCC1OC(=O)C(O)=C1O ZZZCUOFIHGPKAK-UHFFFAOYSA-N 0.000 claims description 19
- 229930003268 Vitamin C Natural products 0.000 claims description 19
- 235000019154 vitamin C Nutrition 0.000 claims description 19
- 239000011718 vitamin C Substances 0.000 claims description 19
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 18
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 claims description 12
- 239000007864 aqueous solution Substances 0.000 claims description 10
- 210000003097 mucus Anatomy 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 6
- 239000007800 oxidant agent Substances 0.000 claims description 6
- 235000010265 sodium sulphite Nutrition 0.000 claims description 6
- DKIDEFUBRARXTE-UHFFFAOYSA-N 3-mercaptopropanoic acid Chemical compound OC(=O)CCS DKIDEFUBRARXTE-UHFFFAOYSA-N 0.000 claims description 5
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 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 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 2
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims description 2
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethyl mercaptane Natural products CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 claims description 2
- 235000001727 glucose Nutrition 0.000 claims description 2
- 239000008103 glucose Substances 0.000 claims description 2
- 235000006408 oxalic acid Nutrition 0.000 claims description 2
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims description 2
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Substances [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- NJRXVEJTAYWCQJ-UHFFFAOYSA-N thiomalic acid Chemical compound OC(=O)CC(S)C(O)=O NJRXVEJTAYWCQJ-UHFFFAOYSA-N 0.000 claims description 2
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical group OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 claims description 2
- 150000001735 carboxylic acids Chemical class 0.000 claims 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 238000010189 synthetic method Methods 0.000 claims 1
- 230000014759 maintenance of location Effects 0.000 abstract description 8
- 238000007334 copolymerization reaction Methods 0.000 abstract description 5
- 239000012966 redox initiator Substances 0.000 abstract description 3
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 abstract description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 abstract description 2
- 239000002904 solvent Substances 0.000 abstract description 2
- 229920000642 polymer Polymers 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 28
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 21
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 18
- 230000015572 biosynthetic process Effects 0.000 description 9
- 238000003786 synthesis reaction Methods 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- 239000004568 cement Substances 0.000 description 7
- 238000010907 mechanical stirring Methods 0.000 description 7
- 239000011259 mixed solution Substances 0.000 description 7
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000008030 superplasticizer Substances 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 3
- 239000003999 initiator Substances 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 2
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- BYDRTKVGBRTTIT-UHFFFAOYSA-N 2-methylprop-2-en-1-ol Chemical compound CC(=C)CO BYDRTKVGBRTTIT-UHFFFAOYSA-N 0.000 description 1
- HNVRRHSXBLFLIG-UHFFFAOYSA-N 3-hydroxy-3-methylbut-1-ene Chemical group CC(C)(O)C=C HNVRRHSXBLFLIG-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- ACIAHEMYLLBZOI-ZZXKWVIFSA-N Unsaturated alcohol Chemical compound CC\C(CO)=C/C ACIAHEMYLLBZOI-ZZXKWVIFSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000007046 ethoxylation reaction Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000005227 gel permeation chromatography Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 125000005394 methallyl group Chemical group 0.000 description 1
- PSZYNBSKGUBXEH-UHFFFAOYSA-M naphthalene-1-sulfonate Chemical compound C1=CC=C2C(S(=O)(=O)[O-])=CC=CC2=C1 PSZYNBSKGUBXEH-UHFFFAOYSA-M 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
Classifications
-
- 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
- C04B24/28—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C04B24/32—Polyethers, e.g. alkylphenol polyglycolether
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
本发明提供了一种异戊二烯基聚醚类聚羧酸盐减水剂,它是异戊二烯基聚氧乙烯醚或异戊二烯基聚氧乙烯丙烯醚(大单体A)与不饱和羧酸及其衍生物(小单体B)的聚合物,属于混凝土外加剂领域。其合成方法是以水为溶剂在较低的温度下将大单体A和小单体B采用氧化还原引发体系引发,在链转移剂作用下经共聚反应而得。这种减水剂克服了烯丙基聚氧乙烯醚合成的减水剂的减水率低,保坍性差,凝结时间长等缺点,具有高保坍,大减水,对混凝土凝结时间影响小的优点。The present invention provides a kind of isoprenyl polyether polycarboxylate water reducer, which is isoprenyl polyoxyethylene ether or isoprenyl polyoxyethylene propylene ether (macromonomer A) The polymer with unsaturated carboxylic acid and its derivative (small monomer B) belongs to the field of concrete admixture. The synthesis method is that the large monomer A and the small monomer B are initiated by a redox initiation system at a relatively low temperature with water as a solvent, and are obtained through copolymerization under the action of a chain transfer agent. This kind of water reducing agent overcomes the disadvantages of low water reducing rate, poor slump retention, and long setting time of the water reducing agent synthesized by allyl polyoxyethylene ether. It has high slump retention, large water reduction, and little influence on the setting time of concrete. advantage.
Description
技术领域 technical field
本发明涉及混凝土减水剂,具体属于一种异戊二烯基聚醚类聚羧酸盐减水剂及其合成方法。The invention relates to a concrete water reducer, in particular to an isoprenyl polyether polycarboxylate water reducer and a synthesis method thereof.
背景技术 Background technique
减水剂用于混凝土,可减少水泥硬化所需要的水分,对水泥具有很强的分散作用,使凝固后混凝土的物理结构更加均匀,提高混凝土的强度。减水剂的发展主要有三个阶段:第一代是以木质素磺酸盐为代表的普通减水剂;第二代是以萘磺酸盐为代表的高效减水剂;第三代是以聚羧酸盐为代表的高性能减水剂。The water reducing agent is used in concrete, which can reduce the water required for cement hardening, has a strong dispersion effect on cement, makes the physical structure of concrete more uniform after solidification, and improves the strength of concrete. The development of water reducers mainly has three stages: the first generation is an ordinary water reducer represented by lignosulfonate; the second generation is a high-efficiency water reducer represented by naphthalene sulfonate; the third generation is a High-performance water reducer represented by polycarboxylate.
带有聚醚侧链的聚羧酸盐减水剂是目前的最新研究成果,它在低掺量下就具有较高的分散性能,良好的保坍性能;另外,它在分子结构上自由度大,合成技术方法多样,获得高性能的潜力巨大。The polycarboxylate superplasticizer with polyether side chain is the latest research achievement at present, it has high dispersion performance and good slump retention performance at low dosage; in addition, its degree of freedom in molecular structure Large, diverse synthesis techniques, great potential for high performance.
目前国内外聚羧酸盐高性能减水剂的专利文献主要是不饱和醇的聚醚类聚羧酸盐减水剂。(甲基)丙烯酸的酯化类减水剂减水率较高,保坍性也好,但是聚酯大单体首先要进行大分子醇和小分子不饱和酸的酯化反应,本步合成难度大,中间分离纯化过程比较复杂,合成出的大分子单体原料不稳定,工业化成本较高。而不饱和醇的聚醚类聚羧酸盐减水剂的合成工艺简单,不饱和聚醚大单体主要通过工业乙氧基化反应设备进行,只需要进行一步开环聚合,不需进行分离,产品纯度很高,后续的聚合工艺简单,目前市场上的产品主要是烯丙基聚氧乙烯醚,该类聚醚活性较低,只能与马来酸酐进行较好的共聚,合成的产品减水率低,保坍性能一般并且由于马来酸酐的双羧基,使的该类聚羧酸盐减水剂对水泥的水化影响较大;目前有报道的产品是甲基烯丙基聚氧乙烯醚,该类聚醚活性较高,能与丙烯酸类小单体进行较好的共聚,合成的减水剂减水率较高,保坍性能好,与各种水泥适应性好。但是其合成时所使用的起始剂为甲基烯丙醇合成工艺复杂,价格较高,属于精细化工品,限制了其大量推广使用。At present, the patent documents of polycarboxylate high-performance water reducers at home and abroad are mainly polyether polycarboxylate water reducers of unsaturated alcohols. The esterification water reducer of (meth)acrylic acid has a high water reducing rate and good slump retention, but the polyester macromonomer must first undergo the esterification reaction of a macromolecular alcohol and a small molecule unsaturated acid, and this step is difficult to synthesize Large, the intermediate separation and purification process is relatively complicated, the raw material of the synthesized macromonomer is unstable, and the industrialization cost is relatively high. The synthesis process of polyether polycarboxylate superplasticizer of unsaturated alcohol is simple. The unsaturated polyether macromonomer is mainly carried out through industrial ethoxylation reaction equipment, and only one-step ring-opening polymerization is required without separation. , the product has high purity, and the follow-up polymerization process is simple. The products currently on the market are mainly allyl polyoxyethylene ethers. This type of polyether has low activity and can only be better copolymerized with maleic anhydride. The synthesized product The water-reducing rate is low, the slump-retaining performance is general, and due to the dicarboxylic groups of maleic anhydride, this type of polycarboxylate superplasticizer has a greater impact on the hydration of cement; the currently reported product is methallyl poly Oxyethylene ether, this type of polyether has high activity and can be well copolymerized with small acrylic monomers. The synthesized water reducer has a high water reducing rate, good slump retention performance, and good adaptability to various cements. However, the initiator used in its synthesis is methallyl alcohol, which has a complicated synthesis process and high price, and belongs to fine chemicals, which limits its large-scale promotion and use.
发明内容 Contents of the invention
本发明的目的是提供一种异戊二烯基聚醚类聚羧酸盐减水剂及其合成方法,该减水剂使用的大单体不仅活性较高,能与丙烯酸类小单体进行较好的共聚,合成的减水剂减水率较高,保坍性能好,与各种水泥适应性好,而且其大单体合成时所使用的起始剂合成工艺简单,价格较低,易于推广。The object of the present invention is to provide a kind of isoprenyl polyether type polycarboxylate water reducer and its synthesis method, the macromonomer used in this water reducer not only has high activity, but also can carry out the reaction with acrylic small monomer Better copolymerization, the synthesized water reducing agent has higher water reducing rate, good slump retention performance, good adaptability to various cements, and the synthesis process of the initiator used in the synthesis of its macromonomer is simple and the price is low. Easy to promote.
本发明提供的一种异戊二烯基聚醚类聚羧酸盐减水剂,它是异戊二烯基聚氧乙烯醚或异戊二烯基聚氧乙烯丙烯醚(A)与不饱和羧酸或其衍生物(B)的聚合物,用式(1)表示大单体A,用式(2)表示小单体B如下:A kind of isoprenyl polyether polycarboxylate water reducing agent provided by the present invention, it is isoprenyl polyoxyethylene ether or isoprenyl polyoxyethylene propylene ether (A) and unsaturated The polymkeric substance of carboxylic acid or derivative (B) thereof, represents macromonomer A with formula (1), represents small monomer B with formula (2) as follows:
其中:R1-氢原子或C原子数为1~5的链烷基Among them: R 1 -hydrogen atom or an alkyl group with 1 to 5 C atoms
m-重复单元数为5~200m-the number of repeating units is 5 to 200
n-重复单元数为0~100,n-the number of repeating units is 0 to 100,
其中:R2-氢原子或C原子数为1~5的链烷基Among them: R 2 -hydrogen atom or an alkyl group with 1 to 5 C atoms
R3-羟基、胺基或C原子数为1~5的链烷基。R 3 -hydroxyl group, amino group or an alkyl group with 1 to 5 C atoms.
合成上述的聚羧酸盐高性能减水剂是将大单体A和小单体B采用氧化还原引发体系引发,在链转移剂作用下经共聚反应而得。The synthesis of the above polycarboxylate high-performance water reducer is obtained by initiating the macromonomer A and small monomer B with a redox initiation system, and undergoing a copolymerization reaction under the action of a chain transfer agent.
具体步骤包括:将大单体A溶解在去离子水中,边搅拌边升温,当温度升到30-50℃时,加入氧化剂,温度达到60-80℃时,同时滴加小单体B水溶液和还原剂与链转移剂的混合水溶液,小单体B水溶液滴加时间控制在2~4小时,还原剂与链转移剂的混合水溶液滴加时间控制在2.5~5小时,滴加完毕后,继续保温0.5~2小时,然后冷却到40℃以下,加入氢氧化钠水溶液进行中和,控制产品浓度为20~50%,pH=6~8,最终得到浅黄色透明粘液;The specific steps include: dissolving the macromonomer A in deionized water, heating up while stirring, when the temperature rises to 30-50°C, adding an oxidant, and when the temperature reaches 60-80°C, simultaneously dropwise adding the small monomer B aqueous solution and For the mixed aqueous solution of reducing agent and chain transfer agent, the time for adding the small monomer B aqueous solution is controlled within 2 to 4 hours, and the time for adding the mixed aqueous solution of reducing agent and chain transfer agent is controlled for 2.5 to 5 hours. After the addition is completed, continue Keep warm for 0.5-2 hours, then cool to below 40°C, add sodium hydroxide aqueous solution to neutralize, control the product concentration to 20-50%, pH=6-8, and finally obtain light yellow transparent mucus;
所述大单体A和小单体B的摩尔比为1∶1~5;The molar ratio of the macromonomer A to the small monomer B is 1:1 to 5;
所述氧化剂和还原剂的总用量占大单体A和小单体B总重量的0.2~5%;The total amount of the oxidizing agent and reducing agent accounts for 0.2-5% of the total weight of the macromonomer A and small monomer B;
所述的链转移剂用量占大单体A和小单体B总重量的0.05~0.25%。The amount of the chain transfer agent accounts for 0.05-0.25% of the total weight of the macromonomer A and the small monomer B.
所述的链转移剂为巯基乙醇、巯基乙酸、巯基丙酸或巯基丁二酸。The chain transfer agent is mercaptoethanol, mercaptoacetic acid, mercaptopropionic acid or mercaptosuccinic acid.
所述的氧化剂可以为过硫酸铵、过硫酸钾、过硫酸钠、双氧水中的一种或几种。The oxidizing agent can be one or more of ammonium persulfate, potassium persulfate, sodium persulfate and hydrogen peroxide.
所述的还原剂可以为维生素C、亚硫酸钠、草酸、葡萄糖中的一种或几种。The reducing agent can be one or more of vitamin C, sodium sulfite, oxalic acid and glucose.
聚羧酸盐减水剂性能测试按照GB8076-2008和GB8077-2000Polycarboxylate superplasticizer performance test according to GB8076-2008 and GB8077-2000
聚羧酸盐减水剂分子量用水相凝胶色谱仪进行检测,分子量5000~200000。The molecular weight of the polycarboxylate water reducer is detected by aqueous gel chromatography, and the molecular weight is 5,000-200,000.
与现有技术相比本发明的优点和效果:本发明使用的大单体是异戊二烯基聚氧乙烯醚,不仅活性较高,能与丙烯酸类小单体进行较好的共聚,合成的减水剂减水率较高,保坍性能好,与各种水泥适应性好,而且其大单体合成时所使用的起始剂为异戊二烯醇,合成工艺简单,价格较低,易于推广。本发明采用了氧化还原引发体系,以水为溶剂合成了一种高效的聚醚类聚羧酸盐高性能减水剂,其生产工艺简单,聚合温度低,所得聚羧酸盐减水剂性能优越。Compared with the prior art, the advantages and effects of the present invention: the macromonomer used in the present invention is isoprenyl polyoxyethylene ether, which not only has high activity, but also can carry out better copolymerization with acrylic small monomers, and synthesizes The water-reducing agent has a high water-reducing rate, good slump-retaining performance, and good adaptability to various cements, and the initiator used in the synthesis of its macromonomer is isoprenyl alcohol, the synthesis process is simple, and the price is low , easy to promote. The present invention adopts a redox initiation system and synthesizes a high-efficiency polyether polycarboxylate superplasticizer with water as a solvent. The production process is simple, the polymerization temperature is low, and the obtained polycarboxylate superplasticizer has excellent performance superior.
具体实施方式 Detailed ways
本发明下述实例中共聚所用的大单体A:Macromonomer A used for the copolymerization of the following examples of the present invention:
IB-500:异戊二烯基聚氧乙烯醚,平均分子量为500;IB-500: Isoprenyl polyoxyethylene ether, the average molecular weight is 500;
IB-1000:异戊二烯基聚氧乙烯醚,平均分子量为1000;IB-1000: Isoprenyl polyoxyethylene ether, the average molecular weight is 1000;
IB-1500:异戊二烯基聚氧乙烯醚,平均分子量为1500;IB-1500: Isoprenyl polyoxyethylene ether, the average molecular weight is 1500;
IB-2000:异戊二烯基聚氧乙烯醚,平均分子量为2000;IB-2000: Isoprenyl polyoxyethylene ether, the average molecular weight is 2000;
IB-2500:异戊二烯基聚氧乙烯醚,平均分子量为2500;IB-2500: Isoprenyl polyoxyethylene ether, the average molecular weight is 2500;
IB-3000:异戊二烯基聚氧乙烯醚,平均分子量为3000;IB-3000: Isoprenyl polyoxyethylene ether, the average molecular weight is 3000;
IB-5000:异戊二烯基聚氧乙烯丙烯醚,平均分子量为4000;IB-5000: Isoprenyl polyoxyethylene propylene ether, the average molecular weight is 4000;
下述实例中所用的小单体B为丙烯酸或甲基丙烯酸。The small monomer B used in the following examples is acrylic acid or methacrylic acid.
实施例1Example 1
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入150gIB-500,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.1g30%的双氧水,在温度达到60℃时,开始同时滴加丙烯酸溶液(22g丙烯酸溶解在10g去离子水中)和维生素C与巯基乙酸的混合溶液(0.5g维生素C、0.3g巯基乙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(6.9g氢氧化钠溶解在71.1g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为40000,密度为1.07g/ml。Add 150g of IB-500 and 120g of deionized water into a 1000ml four-neck flask equipped with mechanical stirring, temperature controller, and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.1g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop acrylic acid solution (22g acrylic acid dissolved in 10g deionized water) and a mixed solution of vitamin C and thioglycolic acid (0.5g vitamin C, 0.3g thioglycolic acid dissolved in 60g deionized water) ), the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (6.9g sodium hydroxide is dissolved in 71.1g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. After testing, the average molecular weight is 40000, and the density is 1.07g/ml.
实施例2Example 2
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入155gIB-1000,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.0g30%的双氧水,在温度达到60℃时,开始同时滴加丙烯酸溶液(16g丙烯酸溶解在10g去离子水中)和亚硫酸钠与巯基乙酸的混合溶液(0.4g亚硫酸钠、0.2g巯基丙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(5.0g氢氧化钠溶解在68.6g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为43000,密度为1.07g/ml。Add 155g of IB-1000 and 120g of deionized water into a 1000ml four-necked flask equipped with mechanical stirring, temperature controller and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.0g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop acrylic acid solution (16g acrylic acid dissolved in 10g deionized water) and a mixed solution of sodium sulfite and thioglycolic acid (0.4g sodium sulfite, 0.2g mercaptopropionic acid dissolved in 60g deionized water) , the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (5.0g sodium hydroxide is dissolved in 68.6g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. After testing, the average molecular weight is 43000, and the density is 1.07g/ml.
实施例3Example 3
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入156gIB-1500,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.1g30%的双氧水,在温度达到60℃时,开始同时滴加甲基丙烯酸溶液(17g甲基丙烯酸溶解在10g去离子水中)和维生素C与巯基乙酸的混合溶液(0.52g维生素C、0.26g巯基乙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(5.3g氢氧化钠溶解在71.9g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为44000,密度为1.07g/ml。Add 156g of IB-1500 and 120g of deionized water into a 1000ml four-necked flask equipped with mechanical stirring, temperature controller, and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.1g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop methacrylic acid solution (17g methacrylic acid dissolved in 10g deionized water) and a mixed solution of vitamin C and thioglycolic acid (0.52g vitamin C, 0.26g thioglycolic acid dissolved in 60g deionized water), the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (5.3g sodium hydroxide is dissolved in 71.9g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. After testing, the average molecular weight is 44000, and the density is 1.07g/ml.
实施例4Example 4
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入165gIB-2000,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.3g30%的双氧水,在温度达到60℃时,开始同时滴加丙烯酸溶液(16.5g丙烯酸溶解在10g去离子水中)和维生素C与巯基乙酸的混合溶液(0.48g维生素C、0.18g巯基丙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(5.2g氢氧化钠溶解在84.2g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为46000,密度为1.07g/ml。Add 165g of IB-2000 and 120g of deionized water into a 1000ml four-necked flask equipped with mechanical stirring, temperature controller and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.3g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop acrylic acid solution (16.5g acrylic acid dissolved in 10g deionized water) and a mixed solution of vitamin C and thioglycolic acid (0.48g vitamin C, 0.18g mercaptopropionic acid dissolved in 60g deionized water) deionized water), the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (5.2g sodium hydroxide is dissolved in 84.2g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. After testing, the average molecular weight is 46000, and the density is 1.07g/ml.
实施例5Example 5
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入178gIB-2500,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.2g30%的双氧水,在温度达到60℃时,开始同时滴加丙烯酸溶液(16.7g丙烯酸溶解在10g去离子水中)和亚硫酸钠与巯基乙酸的混合溶液(0.53g亚硫酸钠、0.27g巯基乙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(5.2g氢氧化钠溶解在104.3g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为49000,密度为1.07g/ml。Add 178g of IB-2500 and 120g of deionized water into a 1000ml four-neck flask equipped with mechanical stirring, temperature controller and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.2g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop acrylic acid solution (16.7g acrylic acid dissolved in 10g deionized water) and a mixed solution of sodium sulfite and thioglycolic acid (0.53g sodium sulfite, 0.27g thioglycolic acid dissolved in 60g deionized water) , the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (5.2g sodium hydroxide is dissolved in 104.3g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. After testing, the average molecular weight is 49000, and the density is 1.07g/ml.
实施例6Example 6
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入187gIB-3000,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.3g30%的双氧水,在温度达到60℃时,开始同时滴加丙烯酸溶液(21g丙烯酸溶解在10g去离子水中)和维生素C与巯基乙酸的混合溶液(0.45g维生素C、0.13g巯基丙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(6.6g氢氧化钠溶解在124.5g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为81000,密度为1.07g/ml。Add 187g of IB-3000 and 120g of deionized water into a 1000ml four-neck flask equipped with mechanical stirring, temperature controller, and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.3g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop acrylic acid solution (21g acrylic acid dissolved in 10g deionized water) and a mixed solution of vitamin C and thioglycolic acid (0.45g vitamin C, 0.13g mercaptopropionic acid dissolved in 60g deionized water) water), the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (6.6g sodium hydroxide is dissolved in 124.5g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. After testing, the average molecular weight is 81000, and the density is 1.07g/ml.
实施例7Example 7
在装有机械搅拌、温度控制器、滴液装置的1000ml四口烧瓶中加入300gIB-5000,同时加入120g去离子水,边搅拌溶解边升温,当温度升到50℃时,加入1.2g30%的双氧水,在温度达到60℃时,开始同时滴加甲基丙烯酸溶液(18g甲基丙烯酸溶解在10g去离子水中)和维生素C与巯基乙酸的混合溶液(0.52g维生素C、0.32g巯基乙酸溶解在60g去离子水中),丙烯酸溶液的滴加时间控制在2.5小时,维生素C溶液的滴加时间控制在3h,反应温度控制在60±2℃。滴加完毕后,继续保温0.5小时,然后冷却到40℃以下,加入氢氧化钠水溶液(5.7g氢氧化钠溶解在289.5g去离子水中)进行中和,得到浓度为40%,pH=7.5的浅黄色透明粘液。经测试平均分子量为53000,密度为1.07g/ml。Add 300g of IB-5000 and 120g of deionized water into a 1000ml four-neck flask equipped with mechanical stirring, temperature controller and dripping device, and heat up while stirring and dissolving. When the temperature rises to 50°C, add 1.2g of 30% Hydrogen peroxide, when the temperature reaches 60°C, start to drop methacrylic acid solution (18g methacrylic acid dissolved in 10g deionized water) and a mixed solution of vitamin C and thioglycolic acid (0.52g vitamin C, 0.32g thioglycolic acid dissolved in 60g deionized water), the dropping time of the acrylic acid solution was controlled at 2.5 hours, the dropping time of the vitamin C solution was controlled at 3 hours, and the reaction temperature was controlled at 60±2°C. After the dropwise addition, continue to insulate for 0.5 hours, then cool to below 40°C, add aqueous sodium hydroxide solution (5.7g sodium hydroxide is dissolved in 289.5g deionized water) to neutralize, and obtain a concentration of 40%, pH=7.5 Pale yellow transparent mucus. The tested average molecular weight is 53000 and the density is 1.07g/ml.
本发明减水剂的评价方法按照GB8076-2008标准进行评价,结果见表1和表2。The evaluation method of the water reducer of the present invention is evaluated according to the GB8076-2008 standard, and the results are shown in Table 1 and Table 2.
表1净浆流动度数据Table 1 Net pulp fluidity data
从表1中可以看出,本发明聚羧酸盐减水剂相对传统的聚醚基聚羧酸盐减水剂,对水泥具有更好的分散性和分散保持性。It can be seen from Table 1 that the polycarboxylate water reducer of the present invention has better dispersibility and dispersion retention for cement than the traditional polyether-based polycarboxylate water reducer.
表2混凝土坍落度数据Table 2 Concrete slump data
从表2中可以看出,本发明聚羧酸盐减水剂相对传统的聚醚基聚羧酸盐减水剂,对混凝土具有更好的分散性和坍落度保持性。It can be seen from Table 2 that the polycarboxylate water reducer of the present invention has better dispersibility and slump retention for concrete than the traditional polyether-based polycarboxylate water reducer.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201010119880 CN101993210B (en) | 2010-03-04 | 2010-03-04 | Prenyl polyether polycarboxylate water reducing agent and synthesis method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201010119880 CN101993210B (en) | 2010-03-04 | 2010-03-04 | Prenyl polyether polycarboxylate water reducing agent and synthesis method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101993210A CN101993210A (en) | 2011-03-30 |
CN101993210B true CN101993210B (en) | 2011-11-09 |
Family
ID=43784037
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201010119880 Active CN101993210B (en) | 2010-03-04 | 2010-03-04 | Prenyl polyether polycarboxylate water reducing agent and synthesis method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101993210B (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102504239A (en) * | 2011-11-03 | 2012-06-20 | 山西合盛邦砼建材有限公司 | Catalyst for preparing polycarboxylate water reducing agent macromonomer and preparation method thereof |
CN102504126B (en) * | 2011-11-03 | 2014-01-01 | 山西合盛邦砼建材有限公司 | Slump loss resistant type gather carboxylate water-reducing agent and preparation method thereof |
CN102910857A (en) * | 2012-08-02 | 2013-02-06 | 烟台市正源防水保温工程有限公司 | Production process of poly carboxylic acid water reducer |
CN102964079A (en) * | 2012-10-11 | 2013-03-13 | 浙江建设职业技术学院 | Low-temperature synthesis method of polyether polycarboxylic acid water reducer |
CN103755208A (en) * | 2013-12-19 | 2014-04-30 | 柳州正菱集团有限公司 | Concrete slump retaining agent |
CN103910831B (en) * | 2014-01-10 | 2017-05-24 | 五家渠格辉新材料有限责任公司 | Method for producing polycarboxylate water reducer from oxalic acid |
CN104276782A (en) * | 2014-08-26 | 2015-01-14 | 泰兴市大愚建筑材料科技发展有限公司 | Polyether type polycarboxylate superplasticizer |
CN104774293B (en) * | 2014-12-17 | 2018-03-20 | 福建路桥翔通建材科技有限公司 | A kind of anti-chamotte mould polycarboxylate water-reducer and preparation method thereof |
CN104961866B (en) * | 2015-06-25 | 2018-01-26 | 甘肃天地华成建材有限公司 | A kind of more amido fibre modification carboxylic acid type water reducing agents and preparation method thereof |
CN104893394A (en) * | 2015-06-25 | 2015-09-09 | 马清浩 | Off-white water-tolerant interior wall putty |
CN104927465A (en) * | 2015-06-25 | 2015-09-23 | 马清浩 | Water-tolerant elastic exterior wall putty and preparing method thereof |
CN106749953A (en) * | 2015-11-20 | 2017-05-31 | 衡阳市银利实业有限公司 | A kind of polycarboxylic acids protects agent of collapsing |
CN106749954A (en) * | 2015-11-20 | 2017-05-31 | 衡阳市银利实业有限公司 | It is a kind of to prepare the method that polycarboxylic acids protects agent of collapsing |
CN105294952B (en) * | 2015-11-24 | 2017-10-31 | 南京红宝丽醇胺化学有限公司 | A kind of preparation method of polycarboxylate water-reducer |
CN106008847A (en) * | 2016-05-19 | 2016-10-12 | 厦门君科建材科技有限公司 | Preparation method of slump retaining ether type polycarboxylic water reducing agent |
CN106008854A (en) * | 2016-06-29 | 2016-10-12 | 武汉市华讯方舟科技有限公司 | Preparation method of polycarboxylic acid water reducing agent |
CN110668758A (en) * | 2019-10-30 | 2020-01-10 | 安徽海螺建材设计研究院有限责任公司 | Grouting material for connecting reinforcing steel bar sleeve |
CN114349915B (en) * | 2022-01-21 | 2023-08-11 | 太原市天鼎恒砼外加剂科技发展有限公司 | Polycarboxylate superplasticizer and preparation method thereof |
CN114671982A (en) * | 2022-02-24 | 2022-06-28 | 浙江鑫月新材料科技有限公司 | A kind of shrinkage-reducing polycarboxylate water-reducing agent and preparation method thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101139414A (en) * | 2006-09-05 | 2008-03-12 | 中国石油天然气集团公司 | Method for synthesizing carboxyl butadiene-styrene latex improving concrete tensile strength |
CN101376576A (en) * | 2008-10-10 | 2009-03-04 | 上海市建筑科学研究院(集团)有限公司 | High-early strength type polycarboxylic acids dehydragent and preparation technique thereof |
-
2010
- 2010-03-04 CN CN 201010119880 patent/CN101993210B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101139414A (en) * | 2006-09-05 | 2008-03-12 | 中国石油天然气集团公司 | Method for synthesizing carboxyl butadiene-styrene latex improving concrete tensile strength |
CN101376576A (en) * | 2008-10-10 | 2009-03-04 | 上海市建筑科学研究院(集团)有限公司 | High-early strength type polycarboxylic acids dehydragent and preparation technique thereof |
Non-Patent Citations (1)
Title |
---|
郑荣华等.异戊二烯/ 甲基丙烯酸甲酯嵌段共聚物的合成与微结构研究.《高分子学报》.1999,(第1期),全文. * |
Also Published As
Publication number | Publication date |
---|---|
CN101993210A (en) | 2011-03-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101993210B (en) | Prenyl polyether polycarboxylate water reducing agent and synthesis method thereof | |
CN103613306B (en) | A kind of poly carboxylic acid series water reducer containing hyperbranched polyamine-ester structure and preparation method thereof | |
CN101974135B (en) | Normal-temperature synthesis method for polycarboxylic acid water-reducing agent | |
CN109354654B (en) | A kind of early strength polycarboxylate water reducer and preparation method thereof | |
CN103772624B (en) | A kind of early-strength type polycarboxylate concrete dehydragent and preparation method thereof | |
CN102887979B (en) | Preparation method of star polycarboxylic acid high-performance water reducing agent | |
CN103980432B (en) | Polycarboxylate water reducer containing modified water-soluble acrylate and preparation method thereof | |
CN103012694B (en) | Preparation method of polyester type pure solid polycarboxylic acid high-performance water reducing agent | |
WO2014085996A1 (en) | Slump retaining polycarboxylic acid superplasticizer | |
CN104193913B (en) | A kind of early-strength polycarboxylate concrete dehydragent and preparation method thereof | |
WO2016026346A1 (en) | Low-temperature method for preparing high-adaptability ether polycarboxylic acid water reducer | |
CN101225148A (en) | A kind of synthetic method of allyl polyether type high performance water reducing agent | |
CN101817657A (en) | Polycarboxylic acid slump retaining agent | |
CN106277899A (en) | A kind of polycarboxylate water-reducer and preparation method thereof | |
CN101353397B (en) | Water-soluble grafting polycarboxylic acids dehydragent and preparation thereof | |
CN102875047B (en) | Polycarboxylic high-efficiency water reducing agent and preparation method thereof | |
CN106699988B (en) | A kind of polycarboxylic-acid polymeric superplasticizer and preparation method thereof | |
CN105061692A (en) | Polyether polycarboxylic acid water reducing agent and preparation method therefor | |
CN106279702A (en) | A kind of froth breaking type function monomer, polycarboxylate water-reducer and preparation method thereof | |
CN101293947A (en) | A kind of preparation method of modified polyacrylic acid graft copolymer high-efficiency water reducer | |
CN102173638A (en) | Polycarboxylate water reducer and preparation method thereof | |
CN107936190A (en) | Four dripping method preparation methods of high diminishing collapse protective poly-carboxylic acid water reducing agent | |
CN101531744A (en) | Method for synthesizing polycarboxylic acid series concrete hyper-dispersant | |
WO2023184785A1 (en) | Crosslinked polycarboxylic acid water reducer and preparation method therefor | |
CN101530760A (en) | Polyether-based polycarboxylic acid series hyper-dispersant and synthetizing method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
ASS | Succession or assignment of patent right |
Owner name: SHANXI HESHENG BANGTONG BUILDING MATERIAL CO., LTD |
|
C41 | Transfer of patent application or patent right or utility model | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20110831 Address after: 030006 Taiyuan, Xiaodian District, Shanxi City Road, No. 92 Applicant after: Shanxi Univeristy Co-applicant after: Shanxi Hesheng Bangtong Building Material Co., Ltd. Address before: 030006 Taiyuan, Xiaodian District, Shanxi City Road, No. 92 Applicant before: Shanxi Univeristy |
|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee | ||
CP01 | Change in the name or title of a patent holder |
Address after: 030006 Taiyuan, Xiaodian District, Shanxi City Road, No. 92 Patentee after: Shanxi Univeristy Patentee after: Shanxi Shan great He Sheng novel material limited-liability company Address before: 030006 Taiyuan, Xiaodian District, Shanxi City Road, No. 92 Patentee before: Shanxi Univeristy Patentee before: Shanxi Hesheng Bangtong Building Material Co., Ltd. |