CN108250370B - Polycarboxylic acid and its use in cement - Google Patents
Polycarboxylic acid and its use in cement Download PDFInfo
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- C08F283/06—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
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- 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
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- C04B2103/00—Function or property of ingredients for mortars, concrete or artificial stone
- C04B2103/30—Water reducers, plasticisers, air-entrainers, flow improvers
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Abstract
Description
技术领域technical field
本发明涉及一种聚羧酸及其在水泥中的用途。The present invention relates to a polycarboxylic acid and its use in cement.
背景技术Background technique
混凝土是世界范围内广泛使用的材料之一,其中水泥作为胶凝材料是其重要组成部分。水泥按性能可分为:1)通用水泥,一般土木建筑工程通常采用的水泥,主要是指:GB175—2007规定的六大类水泥,即硅酸盐水泥、普通硅酸盐水泥、矿渣硅酸盐水泥、火山灰质硅酸盐水泥、粉煤灰硅酸盐水泥和复合硅酸盐水泥;2)专用水泥,是指有专门用途的水泥,如G级油井水泥,道路硅酸盐水泥;3)特性水泥:是指某种性能比较突出的水泥。如:快硬硅酸盐水泥、低热矿渣硅酸盐水泥、膨胀硫铝酸盐水泥、磷铝酸盐水泥和磷酸盐水泥。虽然水泥品种繁多,但是中国及世界上主要使用的还是硅酸盐水泥,即国外统称的波特兰水泥。Concrete is one of the widely used materials in the world, of which cement is an important component as a cementitious material. Cement can be divided into: 1) General cement, cement commonly used in general civil construction projects, mainly refers to: six types of cement specified in GB175-2007, namely Portland cement, ordinary Portland cement, slag silicate Salt cement, pozzolanic Portland cement, fly ash Portland cement and composite Portland cement; 2) Special cement refers to cement with special purpose, such as Grade G oil well cement, road Portland cement; 3 ) characteristic cement: refers to a certain kind of cement with outstanding performance. Such as: fast-hardening Portland cement, low-heat slag Portland cement, expanded sulfoaluminate cement, aluminophosphate cement and phosphate cement. Although there are many kinds of cement, Portland cement is mainly used in China and the world, which is collectively referred to as Portland cement abroad.
作为一种节能环保的新品种,硫铝酸盐水泥逐渐受到越来越多的重视。由于其具有早强快硬、高强、高抗渗、高抗冻、耐腐蚀、低收缩乃至无收缩等优异特性,在一些需要特殊性能的水泥砂浆或混凝土中,获得越来越多的应用,如修补堵漏、注浆灌浆、海工混凝土等。同时,由于硫铝酸盐水泥的生产采用品位较低的矾土、石膏和石灰石为原料,烧制成以无水硫铝酸钙和硅酸二钙为主要矿物组成的熟料,另外掺适量硫酸盐相磨细而成。生产过程具有低能耗、低排放等优点。具有很大的应用推广空间。As a new kind of energy saving and environmental protection, sulfoaluminate cement has gradually received more and more attention. Due to its excellent properties such as early strength and fast hardening, high strength, high impermeability, high frost resistance, corrosion resistance, low shrinkage or even no shrinkage, it has been used in some cement mortars or concretes that require special properties. Such as repair plugging, grouting, marine concrete, etc. At the same time, since the production of sulfoaluminate cement uses low-grade bauxite, gypsum and limestone as raw materials, it is fired into clinker composed of anhydrous calcium sulfoaluminate and dicalcium silicate. The sulfate phase is ground finely. The production process has the advantages of low energy consumption and low emissions. It has a large space for application promotion.
然而,众所周知,水泥砂浆或混凝土的强度、耐久性等很多性能取决于水灰比,即拌合用水量与水泥用量的比值。水灰比越低,通常强度越高,耐久性越好。然而,水灰比的降低同时降低了砂浆或混凝土工作性、流动性等。因此,减水剂,作为一种具有分散水泥颗粒的分散剂,已经成为现代混凝土或砂浆配合比中不可或缺的组分。少量减水剂的加入,可以极大地提高砂浆或混凝土的流动性,减小用水量。尤其是聚羧酸减水剂,由于其很高的减水率(25-40%)、分子结构的多样化及易调控等性能,已经成为目前水泥混凝土减水剂的主要品种。However, it is well known that many properties such as strength and durability of cement mortar or concrete depend on the water-cement ratio, that is, the ratio of mixing water consumption to cement consumption. The lower the water-cement ratio, generally the higher the strength and the better the durability. However, the reduction of the water-cement ratio simultaneously reduces the workability, fluidity, etc. of the mortar or concrete. Therefore, water reducing agent, as a dispersant with dispersed cement particles, has become an indispensable component in the mixing ratio of modern concrete or mortar. The addition of a small amount of water reducing agent can greatly improve the fluidity of mortar or concrete and reduce water consumption. In particular, polycarboxylate superplasticizers have become the main varieties of cement concrete superplasticizers due to their high water-reducing rate (25-40%), diversification of molecular structure and easy regulation and control.
然而,目前市场可得的聚羧酸减水剂多为硅酸盐水泥设计的。不同于硅酸盐水泥,硫铝酸盐水泥组成主要由无水硫铝酸钙、石膏及其它硅酸盐相组成。具有水化速度快、凝结时间快等特点。同时,水泥颗粒及水化产物相的颗粒表面性质不同,导致了传统的聚羧酸减水剂不能成功地应用于硫铝酸盐水泥体系中。主要呈现的问题就是在混凝土中呈现分散性能不足、初始流动度或坍落度小、掺量大、流动保持性或保坍性差等缺点。为此,本专利发明了一种专门应用于硫铝酸盐体系的聚羧酸减水剂。掺入到硫铝酸盐水泥砂浆或混凝土中,具有掺量小、分散性好、保坍性好等优异性能。However, most of the polycarboxylate water reducers currently available in the market are designed for Portland cement. Unlike Portland cement, sulfoaluminate cement is mainly composed of anhydrous calcium sulfoaluminate, gypsum and other silicate phases. It has the characteristics of fast hydration speed and fast setting time. At the same time, the particle surface properties of cement particles and hydration product phases are different, resulting in the inability of traditional polycarboxylate water reducers to be successfully used in sulfoaluminate cement systems. The main problems presented are insufficient dispersibility, low initial fluidity or slump, large admixture, and poor flow retention or slump retention in concrete. To this end, this patent invents a polycarboxylate water reducing agent specially used in sulfoaluminate system. When mixed into sulfoaluminate cement mortar or concrete, it has excellent properties such as small dosage, good dispersibility and good slump retention.
发明内容SUMMARY OF THE INVENTION
针对现有技术存在的缺陷,本发明提供了一种聚羧酸,以及所述聚羧酸在水泥尤其是硫铝酸盐水泥中特别是作为分散剂的应用。在不掺缓凝剂的情况下,本发明提供的聚羧酸作为分散剂能大幅度延长并有效控制对水泥塌落度和流动度的保持,且不泌水,满足工程要求。In view of the defects in the prior art, the present invention provides a polycarboxylic acid and the application of the polycarboxylic acid as a dispersant in cement, especially sulfoaluminate cement. Without adding retarder, the polycarboxylic acid provided by the present invention can greatly prolong and effectively control the maintenance of cement slump and fluidity as a dispersant, without bleeding, and meets engineering requirements.
在第一个方面,本发明提供了一种聚羧酸,其具有梳形结构,且由第一单体A、不饱和羧酸单体B和功能单体C无规共聚而成,其中,所述第一单体选自不饱和聚醚单体和不饱和聚酯单体中的至少一种,各原料的摩尔比为A:B:C=1:(8~50):(0~5),优选地,A:B:C=1:(9~30):(0~5),更优选地,A:B:C=1:(9~30):(0.01~5),更优选地,A:B:C=1:(9~30):(0.5~4)。In a first aspect, the present invention provides a polycarboxylic acid, which has a comb-shaped structure and is formed by random copolymerization of a first monomer A, an unsaturated carboxylic acid monomer B and a functional monomer C, wherein, The first monomer is selected from at least one of unsaturated polyether monomer and unsaturated polyester monomer, and the molar ratio of each raw material is A:B:C=1:(8~50):(0~ 5), preferably, A:B:C=1:(9~30):(0~5), more preferably, A:B:C=1:(9~30):(0.01~5), More preferably, A:B:C=1:(9~30):(0.5~4).
根据本发明的一些实施方式,所述不饱和聚酯单体的结构如式(1)所示,According to some embodiments of the present invention, the structure of the unsaturated polyester monomer is shown in formula (1),
其中:in:
A表示碳原子数为2~4的亚烷基;A represents an alkylene group having 2 to 4 carbon atoms;
B表示碳原子数为2~4且不同于A的亚烷基;B represents an alkylene group having 2 to 4 carbon atoms and different from A;
R1和R2各自独立的表示H或碳原子数为1~5的烷基优选甲基;R 1 and R 2 each independently represent H or an alkyl group having 1 to 5 carbon atoms, preferably a methyl group;
R3表示H或碳原子数为1~4的烷基;R 3 represents H or an alkyl group having 1 to 4 carbon atoms;
X表示碳原子数为0~5的亚烷基;X represents an alkylene group having 0 to 5 carbon atoms;
m表示0~200的整数,优选20~140;m represents an integer from 0 to 200, preferably 20 to 140;
n表示0~200的整数,优选20~140;n represents an integer from 0 to 200, preferably 20 to 140;
m+n>10。m+n>10.
根据本发明的一些实施方式,所述不饱和聚醚单体的结构如式(2)所示,According to some embodiments of the present invention, the structure of the unsaturated polyether monomer is shown in formula (2),
其中:in:
E表示碳原子数为2~4的亚烷基;E represents an alkylene group having 2 to 4 carbon atoms;
F表示碳原子数为2~4且不同于E的亚烷基;F represents an alkylene group having 2 to 4 carbon atoms and is different from E;
R4和R5各自独立的表示H或碳原子数为1~5的烷基优选甲基;R 4 and R 5 each independently represent H or an alkyl group having 1 to 5 carbon atoms, preferably a methyl group;
R6表示H或碳原子数为1~4的烷基;R 6 represents H or an alkyl group having 1 to 4 carbon atoms;
Y表示碳原子数为0~5的亚烷基;Y represents an alkylene group having 0 to 5 carbon atoms;
p表示0~200的整数,优选20~140;p represents an integer from 0 to 200, preferably 20 to 140;
q表示0~200的整数,优选20~140;q represents an integer from 0 to 200, preferably 20 to 140;
p+q>10。p+q>10.
优选地,所述不饱和聚醚单体的分子量为2000~8000,优选为2000~5000。根据一个实施例,所述不饱和聚醚单体为HPEG-4000。Preferably, the molecular weight of the unsaturated polyether monomer is 2000-8000, preferably 2000-5000. According to one embodiment, the unsaturated polyether monomer is HPEG-4000.
优选地,所述不饱和聚酯单体的分子量为2000~8000,优选为2000~5000。Preferably, the molecular weight of the unsaturated polyester monomer is 2000-8000, preferably 2000-5000.
根据本发明的一些实施方式,所述不饱和羧酸单体选自丙烯酸(AA)、甲基丙烯酸、衣康酸、富马酸和马来酸(酐)中的至少一种。According to some embodiments of the present invention, the unsaturated carboxylic acid monomer is selected from at least one of acrylic acid (AA), methacrylic acid, itaconic acid, fumaric acid and maleic acid (anhydride).
根据本发明的一些实施方式,所述功能单体为烯丙基磺酸钠(ALS)、N,N-二甲基乙酰基乙酰胺(DMAA)、2-丙烯酰胺基-2-甲基丙磺酸(AMPS)、对苯乙烯磺酸钠(SSS)、N,N,N-三甲基-3-(2-甲基烯丙酰胺基)-1-氯化丙胺(MAPTAC,CAS号:51410-72-1)、3-甲基丙烯酰氧基丙基三甲氧基硅烷(KH570)和苯乙烯(St)中的至少一种。According to some embodiments of the present invention, the functional monomer is sodium allyl sulfonate (ALS), N,N-dimethylacetylacetamide (DMAA), 2-acrylamido-2-methylpropane Sulfonic acid (AMPS), sodium p-styrenesulfonate (SSS), N,N,N-trimethyl-3-(2-methallylamido)-1-propylamine chloride (MAPTAC, CAS number: 51410-72-1), at least one of 3-methacryloyloxypropyltrimethoxysilane (KH570) and styrene (St).
本发明的第二个方面提供了所述聚羧酸在以硫铝酸盐水泥为主要胶凝材料的砂浆或混凝土中作为分散剂的用途。A second aspect of the present invention provides the use of the polycarboxylic acid as a dispersant in mortar or concrete with sulfoaluminate cement as the main cementitious material.
根据本发明的一些实施方式,所述分散剂不包含其它任何助剂。According to some embodiments of the present invention, the dispersant does not contain any other adjuvants.
根据本发明的一些实施方式,所述分散剂不与缓凝剂同时使用。According to some embodiments of the present invention, the dispersant is not used concurrently with the retarder.
根据本发明的一些实施方式,所述分散剂在所述硫铝酸盐水泥中的掺量为0.1~2.0wt%,优选为0.5~1.5wt%。According to some embodiments of the present invention, the mixing amount of the dispersant in the sulfoaluminate cement is 0.1-2.0 wt %, preferably 0.5-1.5 wt %.
本发明具有以下有益的技术效果:本发明提供的聚羧酸作为硫铝酸盐水泥分散剂,具有提高的减水分散效果,在不掺缓凝剂的情况下,能大幅度延长并有效控制对塌落度和流动度的保持,且不泌水,满足工程要求。The present invention has the following beneficial technical effects: the polycarboxylic acid provided by the present invention, as a dispersant for sulfoaluminate cement, has an improved water-reducing and dispersing effect, and can be greatly extended and effectively controlled without mixing a retarder. The maintenance of slump and fluidity without bleeding meets engineering requirements.
附图说明Description of drawings
图1显示了对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比为10和12时,不同掺量下的初始分散效果。Figure 1 shows the initial dispersion effect at different dosages for the SAC1 cement system with unsaturated carboxylic acid (AA) and macromonomer (HPEG) molar ratios of 10 and 12.
图2显示了对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比小于8或者大于50时,不同掺量下的初始分散效果。Figure 2 shows the initial dispersion effect of different dosages when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (HPEG) is less than 8 or greater than 50 for SAC1 cement system.
图3显示了对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比为10和12时,不同掺量下(0.002表示掺量为0.2wt%、0.005表示掺量为0.5wt%、0.01表示掺量为1wt%、0.015表示掺量为1.5wt%)的流动度保持性。Figure 3 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (HPEG) is 10 and 12, under different dosages (0.002 means the dosage is 0.2wt%, 0.005 means the dosage is 0.5wt%, 0.01 means the dosage is 1wt%, 0.015 means the fluidity retention is 1.5wt%).
图4显示了对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比小于8或者大于50时,不同掺量下的流动度保持性。Figure 4 shows for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (HPEG) is less than 8 or greater than 50, the fluidity retention at different dosages.
图5说明0.5wt%掺量下,不饱和羧酸为AA、大单体为HPEG的时候共聚功能单体分散剂对SAC1体系的流动度保持性。Figure 5 illustrates the fluidity retention of the copolymerized functional monomer dispersant to the SAC1 system when the unsaturated carboxylic acid is AA and the macromonomer is HPEG at a dosage of 0.5 wt%.
图6说明1.5wt%掺量下,不饱和羧酸为AA、大单体为HPEG的时候共聚功能单体分散剂对SAC1体系的流动度保持性。Figure 6 illustrates the fluidity retention of the copolymerized functional monomer dispersant to the SAC1 system when the unsaturated carboxylic acid is AA and the macromonomer is HPEG at a dosage of 1.5 wt%.
图7说明1.5wt%掺量下,不饱和羧酸为AA、大单体为HPEG的时候不同分散剂对SAC2体系的流动度保持性。Figure 7 illustrates the fluidity retention of different dispersants to the SAC2 system when the unsaturated carboxylic acid is AA and the macromonomer is HPEG at a dosage of 1.5 wt%.
图8说明2.0wt%掺量下,不饱和羧酸为AA、大单体为HPEG的时候不同分散剂对SAC2体系的流动度保持性。Figure 8 illustrates the fluidity retention of different dispersants to the SAC2 system when the unsaturated carboxylic acid is AA and the macromonomer is HPEG at a dosage of 2.0 wt%.
图9说明对于SAC1水泥体系,不饱和羧酸(MA)和大单体(HPEG)摩尔比为10和12时,1.5%wt掺量下的初始分散效果。Figure 9 illustrates the initial dispersion effect at 1.5% wt dosage for SAC1 cement system with unsaturated carboxylic acid (MA) and macromonomer (HPEG) molar ratios of 10 and 12.
图10说明对于SAC1水泥体系,不饱和羧酸(MA)和大单体(HPEG)摩尔比为10和12时,不同掺量下的流动度保持性。Figure 10 illustrates the fluidity retention at different dosages for the SAC1 cement system with unsaturated carboxylic acid (MA) and macromonomer (HPEG) molar ratios of 10 and 12.
图11说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(TPEG)摩尔比为10和12时,不同掺量下的初始分散效果。Figure 11 illustrates the initial dispersion effect at different dosages for the SAC1 cement system with unsaturated carboxylic acid (AA) and macromonomer (TPEG) molar ratios of 10 and 12.
图12说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(TPEG)摩尔比为10和12时,1.5%wt掺量下的流动度保持性。Figure 12 illustrates the fluidity retention at 1.5% wt dosage for the SAC1 cement system for unsaturated carboxylic acid (AA) and macromonomer (TPEG) molar ratios of 10 and 12.
具体实施方式Detailed ways
以下结合实施例对本发明进行详细说明,但本发明并不受下述实施例限定。The present invention will be described in detail below with reference to the examples, but the present invention is not limited by the following examples.
本发明采用水溶液自由基共聚法合成聚羧酸。The invention adopts an aqueous solution free radical copolymerization method to synthesize the polycarboxylic acid.
实施例及对比例中所用原料若无特殊说明均为商购获得,分析纯。The raw materials used in the examples and comparative examples were obtained commercially unless otherwise specified, and were analytically pure.
不饱和聚醚单体HPEG购自辽宁奥克化学股份有限公司,分子量为4000。The unsaturated polyether monomer HPEG was purchased from Liaoning Aoke Chemical Co., Ltd., with a molecular weight of 4000.
不饱和聚酯单体TPEG购自辽宁奥克化学股份有限公司,分子量为4000。The unsaturated polyester monomer TPEG was purchased from Liaoning Aoke Chemical Co., Ltd., with a molecular weight of 4000.
PCE为市面上常见的聚羧酸系减水剂。PCE is a common polycarboxylate water reducer on the market.
实施例1Example 1
合成PCE4000-10:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA和24g水混合均匀配制成滴加A,将0.204g3-MPA、0.125gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为29.8%。Synthesis of PCE4000-10: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g of H with a mass concentration of 30% 2 O 2 was added to the three-necked flask. 9g AA and 24g water were mixed uniformly to prepare dropwise A, and 0.204g 3-MPA, 0.125gVc and 25g water were mixed uniformly to prepare dropwise B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 29.8%.
实施例2Example 2
合成PCE4000-12:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将10.8gAA和24g水混合均匀配制成滴加A,将0.241g3-MPA、0.147gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为28.9%。Synthesis of PCE4000-12: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g of H with a mass concentration of 30% 2 O 2 was added to the three-necked flask. 10.8g AA and 24g water were mixed uniformly to prepare dropwise A, and 0.241g 3-MPA, 0.147gVc and 25g water were mixed uniformly to prepare dropwise B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 28.9%.
实施例3Example 3
合成PCE4000-16:称取150g水和80gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.77g质量浓度30%的H2O2加入到三口烧瓶中。将23.04gAA和50g水混合均匀配制成滴加A,将0.505g3-MPA、0.308gVc和30g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为28.4%。Synthesis of PCE4000-16: Weigh 150g of water and 80g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.77g of H with a mass concentration of 30% 2 O 2 was added to the three-necked flask. 23.04g AA and 50g water were mixed uniformly to prepare drop A, and 0.505g 3-MPA, 0.308gVc and 30g water were mixed uniformly to prepare drop B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 28.4%.
实施例4Example 4
合成PCE4000-22:称取150g水和80gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取1.04g质量浓度30%的H2O2加入到三口烧瓶中。将31.68gAA和70g水混合均匀配制成滴加A,将0.684g3-MPA、0.417gVc和35g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为28.6%。Synthesis of PCE4000-22: Weigh 150g of water and 80g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 1.04g of H with a mass concentration of 30% 2 O 2 was added to the three-necked flask. 31.68g AA and 70g water were mixed uniformly to prepare drop A, and 0.684g 3-MPA, 0.417gVc and 35g water were mixed uniformly to prepare drop B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 28.6%.
实施例5Example 5
合成PCE4000-25:称取150g水和80gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取1.18g质量浓度30%的H2O2加入到三口烧瓶中。将36.00gAA和75g水混合均匀配制成滴加A,将0.773g3-MPA、0.471gVc和40g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为29.1%。Synthesis of PCE4000-25: Weigh 150g of water and 80g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 1.18g of H with a mass concentration of 30% 2 O 2 was added to the three-necked flask. 36.00g AA and 75g water were mixed uniformly to prepare drip A, and 0.773g 3-MPA, 0.471gVc and 40g water were mixed uniformly to prepare drip B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 29.1%.
实施例6Example 6
合成PCE4000-30:称取150g水和80gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取1.41g质量浓度30%的H2O2加入到三口烧瓶中。将43.20gAA和90g水混合均匀配制成滴加A,将0.921g3-MPA、0.562gVc和40g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为28.6%。Synthesis of PCE4000-30: Weigh 150g of water and 80g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 1.41g of H with a mass concentration of 30% 2 O 2 was added to the three-necked flask. 43.20g AA and 90g water were mixed uniformly to prepare drip A, and 0.921g 3-MPA, 0.562gVc and 40g water were mixed uniformly to prepare drip B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 28.6%.
实施例7Example 7
合成PCE4000-50:称取82.00g水和50.00gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取1.45g质量浓度30%的H2O2加入到三口烧瓶中。将45.00gAA和95.00g水混合均匀配制成滴加A,将1.35g3-MPA、0.58gVc和45.00g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为29.9%。Synthesis of PCE4000-50: Weigh 82.00g of water and 50.00g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 1.45g of 30% mass concentration The H 2 O 2 was added to the three-necked flask. 45.00g AA and 95.00g water were mixed uniformly to prepare drip A, and 1.35g 3-MPA, 0.58gVc and 45.00g water were mixed uniformly to prepare drip B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 29.9%.
实施例8Example 8
合成PCE4000-10(TPEG):称取82g水和50gTPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA和24g水混合均匀配制成滴加A,将0.204g3-MPA、0.125gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.0%。Synthesis of PCE4000-10 (TPEG): Weigh 82g of water and 50g of TPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g of 30 % H 2 O 2 was added to the three-necked flask. 9g AA and 24g water were mixed uniformly to prepare dropwise A, and 0.204g 3-MPA, 0.125gVc and 25g water were mixed uniformly to prepare dropwise B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 30.0%.
实施例9Example 9
合成PCE4000-12(TPEG):称取82g水和50gTPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将10.8gAA和24g水混合均匀配制成滴加A,将0.241g3-MPA、0.147gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.1%。Synthesis of PCE4000-12 (TPEG): Weigh 82g of water and 50g of TPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g of 30 % H 2 O 2 was added to the three-necked flask. 10.8g AA and 24g water were mixed uniformly to prepare dropwise A, and 0.241g 3-MPA, 0.147gVc and 25g water were mixed uniformly to prepare dropwise B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 30.1%.
实施例10Example 10
合成PCE4000-10-DM-2:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA、2.48gDMAA和33g水混合均匀配制成滴加A,将0.241g3-MPA、0.147gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.0%。Synthesis of PCE4000-10-DM-2: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g for
实施例11Example 11
合成PCE4000-10-MA-2:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA、5.55gMAPTAC和40g水混合均匀配制成滴加A,将0.241g3-MPA、0.147gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为28.1%。Synthesis of PCE4000-10-MA-2: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g for
实施例12Example 12
合成PCE4000-10-AM-2:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA、5.18gAMPS和40g水混合均匀配制成滴加A,将0.241g3-MPA、0.147gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.0%。Synthesis of PCE4000-10-AM-2: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g for
实施例13Example 13
合成PCE4000-10-VPA-2:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA、2.7gVPA和33g水混合均匀配制成滴加A,将0.241g3-MPA、0.147gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为29.8%。Synthesis of PCE4000-10-VPA-2: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g for
实施例14Example 14
合成PCE4000-10-St-0.5:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.33g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA和30g水混合均匀配制成滴加A,将0.21g3-MPA、0.130gVc和25g水混合均匀配制成滴加B,将0.65gSt作为滴加C。滴加A、滴加B和滴加C经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h,滴加C的滴加时间为3h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为26.7%。Synthesis of PCE4000-10-St-0.5: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.33g for
实施例15Example 15
合成PCE4000-10-Si-0.5:称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.33g质量浓度30%的H2O2加入到三口烧瓶中。将9gAA、1.55gKH570和30g水混合均匀配制成滴加A,将0.21g 3-MPA、0.130g Vc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为28.8%。Synthesis of PCE4000-10-Si-0.5: Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.33g for
实施例16Example 16
合成PCE4000-10(MA):称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.31g质量浓度30%的H2O2加入到三口烧瓶中。将12.25gMA和30g水混合均匀配制成滴加A,将0.29g3-MPA、0.12gVc和25g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.1%。Synthesis of PCE4000-10 (MA): Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.31g of 30 % H 2 O 2 was added to the three-necked flask. 12.25g MA and 30g water were mixed uniformly to prepare drop A, and 0.29g 3-MPA, 0.12gVc and 25g water were mixed uniformly to prepare drop B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 30.1%.
实施例17Example 17
合成PCE4000-12(MA):称取82g水和50gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.37g质量浓度30%的H2O2加入到三口烧瓶中。将14.70gMA和35g水混合均匀配制成滴加A,将0.34g3-MPA、0.15gVc和30g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.1%。Synthesis of PCE4000-12 (MA): Weigh 82g of water and 50g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.37g of 30 % H 2 O 2 was added to the three-necked flask. 14.70g MA and 35g water were mixed uniformly to prepare dropwise A, and 0.34g 3-MPA, 0.15gVc and 30g water were mixed uniformly to prepare dropwise B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 30.1%.
对比例1Comparative Example 1
合成PCE4000-5:称取82.00g水和50.00gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取0.17g质量浓度30%的H2O2加入到三口烧瓶中。将4.50gAA和20.00g水混合均匀配制成滴加A,将0.16g3-MPA、0.07gVc和25.00g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为29.9%。Synthesis of PCE4000-5: Weigh 82.00g of water and 50.00g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 0.17g of 30% mass concentration The H 2 O 2 was added to the three-necked flask. 4.50g AA and 20.00g water were mixed uniformly to prepare drip A, and 0.16g 3-MPA, 0.07gVc and 25.00g water were mixed uniformly to prepare drip B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 29.9%.
对比例2Comparative Example 2
合成PCE4000-60:称取82.00g水和50.00gHPEG,溶解混合均匀,倒入恒温水浴锅内的三口烧瓶,搅拌桨以150rpm的转速匀速搅拌并升温至65℃,称取1.73g质量浓度30%的H2O2加入到三口烧瓶中。将54.00gAA和110.00g水混合均匀配制成滴加A,将1.62g3-MPA、0.69gVc和50.00g水混合均匀配制成滴加B。滴加A和滴加B经蠕动泵匀速滴加到三口烧瓶中,滴加A的滴加时间为3h,滴加B的滴加时间为3.5h。滴加完成后,保温1h。反应结束后进行实际固含量测试,测试结果为30.0%。Synthesis of PCE4000-60: Weigh 82.00g of water and 50.00g of HPEG, dissolve and mix evenly, pour into a three-necked flask in a constant temperature water bath, stir with a stirring paddle at a constant speed of 150rpm and heat up to 65°C, weigh 1.73g of 30% mass concentration The H 2 O 2 was added to the three-necked flask. 54.00g AA and 110.00g water were mixed uniformly to prepare dripping A, and 1.62g 3-MPA, 0.69gVc and 50.00g water were mixed uniformly to prepare dripping B. Dropwise A and dropwise B were added dropwise to the three-necked flask through a peristaltic pump at a constant speed, the dropwise addition time of dropwise A was 3h, and the dropwise addition of B was 3.5h. After the dropwise addition was completed, the temperature was kept for 1 h. After the reaction, the actual solid content test was carried out, and the test result was 30.0%.
表1Table 1
性能测试Performance Testing
参照GBT《混凝土外加剂均质性试验方法》,在0.35水灰比条件下,测定对比例1-2和实施例1-17的净浆初始流动度和保持性,实验测试了两种硫铝酸盐水泥,分别用代号SAC1和SAC2表示,其中SAC1和SAC2的成分见下表。检测结果如附图1-12所示。Referring to GBT "Concrete Admixture Homogeneity Test Method", under the condition of 0.35 water-cement ratio, the initial fluidity and retention of the net paste of Comparative Example 1-2 and Example 1-17 were measured, and two kinds of sulfur-aluminum The acid salt cement is represented by the codes SAC1 and SAC2 respectively, and the components of SAC1 and SAC2 are shown in the table below. The test results are shown in Figures 1-12.
表2两种硫铝酸盐水泥化学组成.(wt.%)Table 2 Chemical composition of two sulfoaluminate cements. (wt.%)
图1说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比为10和12时,不同掺量下初始分散效果均优于市面上常用减水剂。Figure 1 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (HPEG) is 10 and 12, the initial dispersion effect at different dosages is better than that of commonly used water reducers on the market.
图2说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比小于8或者大于50时,不同掺量下初始分散效果均较差。Figure 2 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (HPEG) is less than 8 or greater than 50, the initial dispersion effect is poor at different dosages.
图3说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比为10和12时,不同掺量下(0.2%、0.5%、1.0%和1.5%)流动度保持性均优于市面上常用减水剂。Figure 3 illustrates the retention of fluidity at different dosages (0.2%, 0.5%, 1.0% and 1.5%) for the SAC1 cement system with a molar ratio of unsaturated carboxylic acid (AA) to macromonomer (HPEG) of 10 and 12. The properties are better than the commonly used water reducers on the market.
图4说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(HPEG)摩尔比小于8或者大于50时,不同掺量下流动度保持性均较差。Figure 4 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (HPEG) is less than 8 or greater than 50, the fluidity retention is poor at different dosages.
图5说明0.5%掺量下,不饱和羧酸为AA、大单体为HPEG的时候共聚功能单体分散剂对SAC1体系的流动度保持性均优于市面上常用减水剂。Figure 5 shows that at 0.5% dosage, when the unsaturated carboxylic acid is AA and the macromonomer is HPEG, the fluidity retention of the copolymerized functional monomer dispersant to the SAC1 system is better than that of the commonly used water reducers on the market.
图6说明1.5%掺量下,不饱和羧酸为AA、大单体为HPEG的时候共聚功能单体分散剂对SAC1体系的流动度保持性均优于市面上常用减水剂。Figure 6 shows that at 1.5% dosage, when the unsaturated carboxylic acid is AA and the macromonomer is HPEG, the fluidity retention of the copolymerized functional monomer dispersant to the SAC1 system is better than that of the commonly used water reducers on the market.
图7说明1.5%掺量下,不饱和羧酸为AA、大单体为HPEG的时候不同分散剂对SAC2体系的流动度保持性均优于市面上常用减水剂。Figure 7 shows that under the dosage of 1.5%, when the unsaturated carboxylic acid is AA and the macromonomer is HPEG, the fluidity retention of different dispersants to the SAC2 system is better than that of the commonly used water reducers on the market.
图8说明2.0%掺量下,不饱和羧酸为AA、大单体为HPEG的时候不同分散剂对SAC2体系的流动度保持性均优于市面上常用减水剂。Figure 8 shows that under the dosage of 2.0%, when the unsaturated carboxylic acid is AA and the macromonomer is HPEG, the fluidity retention of different dispersants to the SAC2 system is better than that of the commonly used water reducers on the market.
图9说明对于SAC1水泥体系,不饱和羧酸(MA)和大单体(HPEG)摩尔比为10和12时,1.5%掺量下,初始分散效果均优于市面上常用减水剂。Figure 9 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (MA) and macromonomer (HPEG) is 10 and 12, the initial dispersion effect at 1.5% dosage is better than that of commonly used water reducers on the market.
图10说明对于SAC1水泥体系,不饱和羧酸(MA)和大单体(HPEG)摩尔比为10和12时,不同掺量下流动度保持性均优于市面上常用减水剂。Figure 10 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (MA) and macromonomer (HPEG) is 10 and 12, the fluidity retention at different dosages is better than that of commonly used water reducers on the market.
图11说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(TPEG)摩尔比为10和12时,不同掺量下初始分散效果均优于市面上常用减水剂。Figure 11 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (TPEG) is 10 and 12, the initial dispersion effect under different dosages is better than that of commonly used water reducers on the market.
图12说明对于SAC1水泥体系,不饱和羧酸(AA)和大单体(TPEG)摩尔比为10和12时,1.5%掺量下,流动度保持性均优于市面上常用减水剂。Figure 12 shows that for the SAC1 cement system, when the molar ratio of unsaturated carboxylic acid (AA) and macromonomer (TPEG) is 10 and 12, the fluidity retention at 1.5% dosage is better than that of commonly used water reducers on the market.
虽然本发明已作了详细描述,但对本领域技术人员来说,在本发明精神和范围内的修改将是显而易见的。此外,应当理解的是,本发明记载的各方面、不同具体实施方式的各部分和列举的各种特征可被组合或全部或部分互换。在上述的各个具体实施方式中,那些参考另一个具体实施方式的实施方式可适当地与其它实施方式组合,这是将由本领域技术人员所能理解的。此外,本领域技术人员将会理解,前面的描述仅是示例的方式,并不旨在限制本发明。Although the invention has been described in detail, modifications within the spirit and scope of the invention will be apparent to those skilled in the art. Furthermore, it is to be understood that the various described aspects, parts of the various embodiments, and various features recited may be combined or interchanged in whole or in part. In each of the above-described embodiments, those referring to another embodiment may be appropriately combined with other embodiments, as will be understood by those skilled in the art. Furthermore, those skilled in the art will appreciate that the foregoing description is by way of example only, and is not intended to limit the present invention.
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