CN111378135A - A kind of preparation method of low-viscosity alkoxy-terminated polydimethylsiloxane - Google Patents
A kind of preparation method of low-viscosity alkoxy-terminated polydimethylsiloxane Download PDFInfo
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Abstract
本发明提供一种低粘度烷氧基封端聚二甲基硅氧烷的制备方法,包括以下步骤:(1)将DMC和六甲基二硅氧烷混合后升温,滴加入磷酸,搅拌回流除水得到硅磷酸酯终止剂;(2)将线性体升温,加入氢氧化钾水溶液后搅拌缩聚反应,加入硅磷酸酯终止剂,继续反应得到羟基硅油;(3)将含氢双封头加入羟基硅油,搅拌至混合均匀,升温加入磷腈催化剂,搅拌反应加入氨气终止剂,继续反应后得到低粘度含氢硅油;(4)将低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂混合,搅拌反应得到低粘度烷氧基封端聚二甲基硅氧烷。本发明制备出的低粘度烷氧基封端聚二甲基硅氧烷具有较低的粘度,以及较好的硬度、断裂伸长率、稳定性。The invention provides a preparation method of low-viscosity alkoxy-terminated polydimethylsiloxane, comprising the following steps: (1) mixing DMC and hexamethyldisiloxane, heating up, adding phosphoric acid dropwise, stirring and refluxing Remove water to obtain silicophosphate terminator; (2) heat up the linear body, add potassium hydroxide aqueous solution, stir the polycondensation reaction, add silicophosphate terminator, and continue the reaction to obtain hydroxy silicone oil; (3) add hydrogen-containing double head to Hydroxy silicone oil, stir until the mixture is uniform, add phosphazene catalyst at the temperature, add ammonia gas terminator to the stirring reaction, and continue the reaction to obtain low-viscosity hydrogen-containing silicone oil; (4) Mix low-viscosity hydrogen-containing silicone oil, vinyltrimethoxysilane, platinum The catalysts are mixed, and the reaction is stirred to obtain a low viscosity alkoxy terminated polydimethylsiloxane. The low-viscosity alkoxy-terminated polydimethylsiloxane prepared by the invention has lower viscosity, better hardness, elongation at break and stability.
Description
技术领域technical field
本发明涉及一种低粘度烷氧基封端聚二甲基硅氧烷的制备方法。The invention relates to a preparation method of low-viscosity alkoxy-terminated polydimethylsiloxane.
背景技术Background technique
聚二甲基硅氧烷(PDMS,polydimethylsiloxane),是一种疏水类的有机硅物料。在药品、日化用品、食品、建筑等各领域均有应用,它的衍生物已达数百种,常用的聚硅氧烷主要有:聚二甲基硅氧烷,环甲基硅氧烷,氨基硅氧烷,聚甲基苯基硅氧烷,聚醚聚硅氧烷共聚物。改性的聚二甲基硅氧烷,是在硅油的支链或主链上通过化学反应,引入不同的官能团,由于各种特殊官能团的引入,赋予改性的聚二甲基硅氧烷更多特殊的优异性能。目前比较常见的作法是对聚二甲基硅氧烷进行封端改性,封端的种类包括端羟基、端甲基、端烷氧基、烯丙基硅基等。Polydimethylsiloxane (PDMS, polydimethylsiloxane) is a hydrophobic silicone material. It has applications in various fields such as medicine, daily chemicals, food, construction, etc. It has hundreds of derivatives. The commonly used polysiloxanes are: polydimethylsiloxane, cyclomethylsiloxane , aminosiloxane, polymethylphenylsiloxane, polyether polysiloxane copolymer. The modified polydimethylsiloxane is a chemical reaction on the branch or main chain of the silicone oil to introduce different functional groups. Due to the introduction of various special functional groups, the modified polydimethylsiloxane is better. Many special excellent performance. At present, a common practice is to perform end-capping modification on polydimethylsiloxane, and the types of end-capping include terminal hydroxyl groups, terminal methyl groups, terminal alkoxy groups, allylsilyl groups, and the like.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题是提供一种低粘度烷氧基封端聚二甲基硅氧烷的制备方法,其制备出的低粘度烷氧基封端聚二甲基硅氧烷具有较低的粘度,以及较好的硬度、断裂伸长率、稳定性。The technical problem to be solved by the present invention is to provide a preparation method of low-viscosity alkoxy-terminated polydimethylsiloxane, and the prepared low-viscosity alkoxy-terminated polydimethylsiloxane has lower viscosity, and good hardness, elongation at break and stability.
为解决上述技术问题,本发明的技术方案是:For solving the above-mentioned technical problems, the technical scheme of the present invention is:
一种低粘度烷氧基封端聚二甲基硅氧烷的制备方法,包括以下步骤:A preparation method of low-viscosity alkoxy-terminated polydimethylsiloxane, comprising the following steps:
(1)将DMC和六甲基二硅氧烷混合后升温至160-180℃,滴加入磷酸,搅拌6-8小时回流除水得到硅磷酸酯终止剂;(1) after mixing DMC and hexamethyldisiloxane, the temperature is raised to 160-180 ℃, phosphoric acid is added dropwise, stirred for 6-8 hours and refluxed to remove water to obtain a silicophosphate terminator;
(2)将线性体升温至130-150℃,加入氢氧化钾水溶液后搅拌缩聚反应,在线监测粘度,达到目标粘度前加入步骤(1)所得硅磷酸酯终止剂,继续反应5-50分钟后抽真空减压蒸馏去除低沸点物质得到羟基硅油;(2) the linear body is heated up to 130-150 ℃, after adding the potassium hydroxide aqueous solution, the polycondensation reaction is stirred, and the viscosity is monitored on-line. Before reaching the target viscosity, the silicophosphate terminator obtained in step (1) is added, and the reaction is continued for 5-50 minutes. Vacuuming and decompression distillation to remove low-boiling substances to obtain hydroxyl silicone oil;
(3)将含氢双封头加入步骤(2)所得羟基硅油,搅拌至混合均匀,升温至55-65℃后加入磷腈催化剂,搅拌反应达到目标粘度后加入氨气终止剂,继续反应3-6小时后抽真空减压蒸馏去除低沸点物质得到低粘度含氢硅油;(3) adding the hydrogen-containing double head to the hydroxy silicone oil obtained in step (2), stirring until the mixture is uniform, adding the phosphazene catalyst after the temperature is raised to 55-65 ° C, adding the ammonia gas terminator after the stirring reaction reaches the target viscosity, and continuing the reaction 3 -After 6 hours, the low-boiling substances are removed by vacuum distillation to obtain low-viscosity hydrogen-containing silicone oil;
(4)将步骤(3)所得低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂混合,搅拌反应得到低粘度烷氧基封端聚二甲基硅氧烷。(4) Mixing the low-viscosity hydrogen-containing silicone oil obtained in step (3), vinyltrimethoxysilane and platinum catalyst, and stirring the reaction to obtain a low-viscosity alkoxy-terminated polydimethylsiloxane.
进一步地,本发明所述步骤(1)中,DMC、六甲基二硅氧烷、磷酸的质量比为(60-80):(5-15):(10-20)。Further, in the step (1) of the present invention, the mass ratio of DMC, hexamethyldisiloxane and phosphoric acid is (60-80):(5-15):(10-20).
进一步地,本发明所述步骤(1)中,搅拌的速度为200-400r/min。Further, in the step (1) of the present invention, the stirring speed is 200-400 r/min.
进一步地,本发明所述步骤(2)中,氢氧化钾水溶液的质量浓度为10%,线性体、氢氧化钾水溶液、硅磷酸酯终止剂的质量比为40000:1:(1.5-2)。Further, in the step (2) of the present invention, the mass concentration of the potassium hydroxide aqueous solution is 10%, and the mass ratio of the linear body, the potassium hydroxide aqueous solution, and the silicophosphate terminator is 40000:1:(1.5-2) .
进一步地,本发明所述步骤(2)中,目标粘度为1000-1500mPa·s。Further, in the step (2) of the present invention, the target viscosity is 1000-1500 mPa·s.
进一步地,本发明所述步骤(3)中,羟基硅油、含氢双封头、磷腈催化剂、氨气终止剂的质量比为(70-90):(10-20):(0.1-0.6):(1-6)。Further, in step (3) of the present invention, the mass ratio of hydroxy silicone oil, hydrogen-containing double-head, phosphazene catalyst, and ammonia gas terminator is (70-90):(10-20):(0.1-0.6 ):(1-6).
进一步地,本发明所述步骤(3)中,搅拌反应时的搅拌速度为400-800r/min。Further, in the step (3) of the present invention, the stirring speed during the stirring reaction is 400-800 r/min.
进一步地,本发明所述步骤(3)中,目标粘度为2500-3000mPa·s。Further, in the step (3) of the present invention, the target viscosity is 2500-3000 mPa·s.
进一步地,本发明所述步骤(4)中,低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂的质量比为(60-80):(20-30):(0.3-0.6)。Further, in step (4) of the present invention, the mass ratio of low-viscosity hydrogen-containing silicone oil, vinyltrimethoxysilane, and platinum catalyst is (60-80):(20-30):(0.3-0.6).
进一步地,本发明所述步骤(4)中,搅拌反应的过程为:先加热至25-35℃搅拌反应30-40分钟,然后加热至70-80℃搅拌反应2-3小时,搅拌反应时的搅拌速度为300-500r/min。Further, in the step (4) of the present invention, the process of the stirring reaction is: firstly heated to 25-35 °C for stirring reaction for 30-40 minutes, then heated to 70-80 °C for stirring reaction for 2-3 hours, when stirring reaction The stirring speed is 300-500r/min.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明将含氢双封头作为功能材料,选用线性体作为基础原料制备得到羟基硅油,然后利用功能材料对聚二甲基硅氧烷进行改性从而制得低粘度含氢硅油,再与乙烯基三甲氧基硅烷在铂金催化剂的作用下加成制得具有较低的粘度,以及较好的硬度、断裂伸长率、稳定性的低粘度烷氧基封端聚二甲基硅氧烷。In the invention, the hydrogen-containing double head is used as the functional material, the linear body is selected as the basic raw material to prepare the hydroxy silicone oil, and then the functional material is used to modify the polydimethylsiloxane to obtain the low-viscosity hydrogen-containing silicone oil, which is then mixed with ethylene The alkoxy-terminated polydimethylsiloxane with low viscosity, good hardness, elongation at break and stability was prepared by addition of alkoxytrimethoxysilane under the action of platinum catalyst.
具体实施方式Detailed ways
下面将结合具体实施例来详细说明本发明,在此本发明的示意性实施例以及说明用来解释本发明,但并不作为对本发明的限定。The present invention will be described in detail below with reference to specific embodiments. The exemplary embodiments and descriptions of the present invention are used to explain the present invention, but are not intended to limit the present invention.
实施例1Example 1
按照以下步骤制备低粘度烷氧基封端聚二甲基硅氧烷:Follow the steps below to prepare low viscosity alkoxy terminated polydimethylsiloxane:
(1)将DMC和六甲基二硅氧烷混合后升温至170℃,滴加入磷酸,300r/min速度下搅拌7小时回流除水得到硅磷酸酯终止剂,DMC、六甲基二硅氧烷、磷酸的质量比为70:10:15;(1) After mixing DMC and hexamethyldisiloxane, the temperature was raised to 170° C., phosphoric acid was added dropwise, and stirring was performed at a speed of 300 r/min for 7 hours to remove water and reflux to obtain a silicophosphate terminator, DMC, hexamethyldisiloxane The mass ratio of alkane and phosphoric acid is 70:10:15;
(2)将线性体升温至140℃,加入质量浓度为10%的氢氧化钾水溶液后搅拌缩聚反应,在线监测粘度,达到目标粘度1200mPa·s前加入步骤(1)所得硅磷酸酯终止剂,继续反应30分钟后抽真空减压蒸馏去除低沸点物质得到羟基硅油,线性体、氢氧化钾水溶液、硅磷酸酯终止剂的质量比为40000:1:1.8;(2) heating the linear body to 140° C., adding a potassium hydroxide aqueous solution with a mass concentration of 10% and then stirring the polycondensation reaction, monitoring the viscosity online, and adding the silicophosphate terminator obtained in step (1) before reaching the target viscosity of 1200 mPa·s, After continuing to react for 30 minutes, the low-boiling substance was removed by vacuum distillation to obtain hydroxy silicone oil, and the mass ratio of linear body, potassium hydroxide aqueous solution, and silicophosphate terminator was 40000:1:1.8;
(3)将含氢双封头加入步骤(2)所得羟基硅油,搅拌至混合均匀,升温至60℃后加入磷腈催化剂,600r/min搅拌速度下搅拌反应达到目标粘度2700mPa·s后加入氨气终止剂,继续反应4小时后抽真空减压蒸馏去除低沸点物质得到低粘度含氢硅油,羟基硅油、含氢双封头、磷腈催化剂、氨气终止剂的质量比为80:15:0.3:3;(3) Add the hydrogen-containing double head to the hydroxy silicone oil obtained in step (2), stir until the mixture is uniform, add the phosphazene catalyst after the temperature is raised to 60 °C, and then add ammonia after the stirring reaction reaches the target viscosity of 2700 mPa·s at a stirring speed of 600 r/min. The gas terminator, vacuuming and decompressing distillation to remove low-boiling substances after continuing to react for 4 hours to obtain low-viscosity hydrogen-containing silicone oil, the mass ratio of hydroxy silicone oil, hydrogen-containing double-head, phosphazene catalyst, and ammonia gas terminator is 80:15: 0.3:3;
(4)将质量比为70:25:0.4的步骤(3)所得低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂混合,先加热至30℃搅拌反应35分钟,然后加热至75℃搅拌反应2.5小时得到低粘度烷氧基封端聚二甲基硅氧烷,搅拌反应时的搅拌速度为400r/min。(4) Mix the low-viscosity hydrogen-containing silicone oil, vinyltrimethoxysilane and platinum catalyst obtained in step (3) with a mass ratio of 70:25:0.4, first heat to 30°C and stir for 35 minutes, and then heat to 75°C The low-viscosity alkoxy-terminated polydimethylsiloxane was obtained by stirring the reaction for 2.5 hours, and the stirring speed during the stirring reaction was 400 r/min.
实施例2Example 2
按照以下步骤制备低粘度烷氧基封端聚二甲基硅氧烷:Follow the steps below to prepare low viscosity alkoxy terminated polydimethylsiloxane:
(1)将DMC和六甲基二硅氧烷混合后升温至160℃,滴加入磷酸,200r/min速度下搅拌8小时回流除水得到硅磷酸酯终止剂,DMC、六甲基二硅氧烷、磷酸的质量比为60:5:10;(1) After mixing DMC and hexamethyldisiloxane, the temperature was raised to 160° C., phosphoric acid was added dropwise, and the water was refluxed for 8 hours under stirring at 200 r/min to obtain a silicophosphate terminator, DMC, hexamethyldisiloxane The mass ratio of alkane and phosphoric acid is 60:5:10;
(2)将线性体升温至130℃,加入质量浓度为10%的氢氧化钾水溶液后搅拌缩聚反应,在线监测粘度,达到目标粘度1000mPa·s前加入步骤(1)所得硅磷酸酯终止剂,继续反应5分钟后抽真空减压蒸馏去除低沸点物质得到羟基硅油,线性体、氢氧化钾水溶液、硅磷酸酯终止剂的质量比为40000:1:1.5;(2) heating the linear body to 130° C., adding a potassium hydroxide aqueous solution with a mass concentration of 10% and then stirring the polycondensation reaction, monitoring the viscosity on-line, and adding the silicophosphate terminator obtained in step (1) before reaching the target viscosity of 1000 mPa·s, After continuing the reaction for 5 minutes, the low-boiling substance was removed by vacuum distillation to obtain hydroxy silicone oil, and the mass ratio of linear body, potassium hydroxide aqueous solution, and silicophosphate terminator was 40000:1:1.5;
(3)将含氢双封头加入步骤(2)所得羟基硅油,搅拌至混合均匀,升温至55℃后加入磷腈催化剂,800r/min搅拌速度下搅拌反应达到目标粘度2500mPa·s后加入氨气终止剂,继续反应6小时后抽真空减压蒸馏去除低沸点物质得到低粘度含氢硅油,羟基硅油、含氢双封头、磷腈催化剂、氨气终止剂的质量比为70:10:0.1:1;(3) Add the hydrogen-containing double head to the hydroxy silicone oil obtained in step (2), stir until the mixture is uniform, add the phosphazene catalyst after the temperature is raised to 55 °C, and then add ammonia after the stirring reaction reaches the target viscosity of 2500 mPa·s at a stirring speed of 800 r/min. Gas terminator, vacuuming and decompressing distillation to remove low-boiling substances after continuing to react for 6 hours to obtain low-viscosity hydrogen-containing silicone oil, the mass ratio of hydroxy silicone oil, hydrogen-containing double-head, phosphazene catalyst, and ammonia gas terminator is 70:10: 0.1:1;
(4)将质量比为60:20:0.3的步骤(3)所得低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂混合,先加热至25℃搅拌反应40分钟,然后加热至70℃搅拌反应3小时得到低粘度烷氧基封端聚二甲基硅氧烷,搅拌反应时的搅拌速度为300r/min。(4) Mix the low-viscosity hydrogen-containing silicone oil, vinyltrimethoxysilane, and platinum catalyst obtained in step (3) with a mass ratio of 60:20:0.3, first heat to 25°C and stir for 40 minutes, and then heat to 70°C The low-viscosity alkoxy-terminated polydimethylsiloxane was obtained by stirring the reaction for 3 hours, and the stirring speed during the stirring reaction was 300 r/min.
实施例3Example 3
按照以下步骤制备低粘度烷氧基封端聚二甲基硅氧烷:Follow the steps below to prepare low viscosity alkoxy terminated polydimethylsiloxane:
(1)将DMC和六甲基二硅氧烷混合后升温至180℃,滴加入磷酸,400r/min速度下搅拌6小时回流除水得到硅磷酸酯终止剂,DMC、六甲基二硅氧烷、磷酸的质量比为80:15:20;(1) After mixing DMC and hexamethyldisiloxane, the temperature was raised to 180° C., phosphoric acid was added dropwise, and stirring was performed at a speed of 400 r/min for 6 hours to remove water under reflux to obtain a silicophosphate terminator, DMC, hexamethyldisiloxane The mass ratio of alkane and phosphoric acid is 80:15:20;
(2)将线性体升温至150℃,加入质量浓度为10%的氢氧化钾水溶液后搅拌缩聚反应,在线监测粘度,达到目标粘度1500mPa·s前加入步骤(1)所得硅磷酸酯终止剂,继续反应50分钟后抽真空减压蒸馏去除低沸点物质得到羟基硅油,线性体、氢氧化钾水溶液、硅磷酸酯终止剂的质量比为40000:1:2;(2) heating the linear body to 150° C., adding a potassium hydroxide aqueous solution with a mass concentration of 10% and then stirring the polycondensation reaction, monitoring the viscosity on-line, and adding the silicophosphate ester terminator obtained in step (1) before reaching the target viscosity of 1500 mPa·s, After continuing the reaction for 50 minutes, the low-boiling substance was removed by vacuum distillation to obtain hydroxy silicone oil, and the mass ratio of linear body, potassium hydroxide aqueous solution, and silicophosphate terminator was 40000:1:2;
(3)将含氢双封头加入步骤(2)所得羟基硅油,搅拌至混合均匀,升温至65℃后加入磷腈催化剂,400r/min搅拌速度下搅拌反应达到目标粘度3000mPa·s后加入氨气终止剂,继续反应3小时后抽真空减压蒸馏去除低沸点物质得到低粘度含氢硅油,羟基硅油、含氢双封头、磷腈催化剂、氨气终止剂的质量比为90:20:0.6:6;(3) Add the hydrogen-containing double head to the hydroxy silicone oil obtained in step (2), stir until the mixture is uniform, add the phosphazene catalyst after the temperature is raised to 65 °C, and then add ammonia after the stirring reaction reaches the target viscosity of 3000 mPa·s at a stirring speed of 400 r/min. Gas terminator, vacuuming and decompressing distillation to remove low-boiling substances after continuing to react for 3 hours to obtain low-viscosity hydrogen-containing silicone oil, the mass ratio of hydroxy silicone oil, hydrogen-containing double-head, phosphazene catalyst, and ammonia gas terminator is 90:20: 0.6:6;
(4)将质量比为80:30:0.6的步骤(3)所得低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂混合,先加热至35℃搅拌反应30分钟,然后加热至80℃搅拌反应2小时得到低粘度烷氧基封端聚二甲基硅氧烷,搅拌反应时的搅拌速度为500r/min。(4) Mix the low-viscosity hydrogen-containing silicone oil, vinyltrimethoxysilane, and platinum catalyst obtained in step (3) with a mass ratio of 80:30:0.6, first heat to 35° C. and stir for 30 minutes, and then heat to 80° C. The low-viscosity alkoxy-terminated polydimethylsiloxane was obtained by stirring the reaction for 2 hours, and the stirring speed during the stirring reaction was 500 r/min.
实施例4Example 4
按照以下步骤制备低粘度烷氧基封端聚二甲基硅氧烷:Follow the steps below to prepare low viscosity alkoxy terminated polydimethylsiloxane:
(1)将DMC和六甲基二硅氧烷混合后升温至175℃,滴加入磷酸,350r/min速度下搅拌7.5小时回流除水得到硅磷酸酯终止剂,DMC、六甲基二硅氧烷、磷酸的质量比为75:12:16;(1) After mixing DMC and hexamethyldisiloxane, the temperature was raised to 175° C., phosphoric acid was added dropwise, and stirring was performed at a speed of 350 r/min for 7.5 hours to remove water under reflux to obtain silicophosphate terminator, DMC, hexamethyldisiloxane The mass ratio of alkane and phosphoric acid is 75:12:16;
(2)将线性体升温至135℃,加入质量浓度为10%的氢氧化钾水溶液后搅拌缩聚反应,在线监测粘度,达到目标粘度1100mPa·s前加入步骤(1)所得硅磷酸酯终止剂,继续反应40分钟后抽真空减压蒸馏去除低沸点物质得到羟基硅油,线性体、氢氧化钾水溶液、硅磷酸酯终止剂的质量比为40000:1:1.6;(2) heating the linear body to 135° C., adding a potassium hydroxide aqueous solution with a mass concentration of 10% and then stirring the polycondensation reaction, monitoring the viscosity online, and adding the silicophosphate terminator obtained in step (1) before reaching the target viscosity of 1100 mPa·s, After continuing to react for 40 minutes, the low-boiling substance was removed by vacuum and reduced pressure distillation to obtain hydroxy silicone oil, and the mass ratio of linear body, potassium hydroxide aqueous solution, and silicophosphate terminator was 40000:1:1.6;
(3)将含氢双封头加入步骤(2)所得羟基硅油,搅拌至混合均匀,升温至60℃后加入磷腈催化剂,500r/min搅拌速度下搅拌反应达到目标粘度2600mPa·s后加入氨气终止剂,继续反应5小时后抽真空减压蒸馏去除低沸点物质得到低粘度含氢硅油,羟基硅油、含氢双封头、磷腈催化剂、氨气终止剂的质量比为85:17:0.5:5;(3) Add the hydrogen-containing double head to the hydroxy silicone oil obtained in step (2), stir until the mixture is uniform, add the phosphazene catalyst after the temperature is raised to 60 °C, and then add ammonia after the stirring reaction reaches the target viscosity of 2600 mPa·s at a stirring speed of 500 r/min. Gas terminator, vacuuming and depressurizing distillation to remove low-boiling substances after continuing to react for 5 hours to obtain low-viscosity hydrogen-containing silicone oil, the mass ratio of hydroxy silicone oil, hydrogen-containing double-head, phosphazene catalyst, and ammonia gas terminator is 85:17: 0.5:5;
(4)将质量比为75:28:0.5的步骤(3)所得低粘度含氢硅油、乙烯基三甲氧基硅烷、铂金催化剂混合,先加热至30℃搅拌反应35分钟,然后加热至75℃搅拌反应2.5小时得到低粘度烷氧基封端聚二甲基硅氧烷,搅拌反应时的搅拌速度为450r/min。(4) Mix the low-viscosity hydrogen-containing silicone oil, vinyltrimethoxysilane and platinum catalyst obtained in step (3) with a mass ratio of 75:28:0.5, first heat to 30°C and stir for 35 minutes, and then heat to 75°C The low-viscosity alkoxy-terminated polydimethylsiloxane was obtained by stirring the reaction for 2.5 hours, and the stirring speed during the stirring reaction was 450 r/min.
对比例1Comparative Example 1
与实施例1不同的是不包括步骤(3)。The difference from Example 1 is that step (3) is not included.
对比例2Comparative Example 2
与实施例1不同的是步骤(4)中的乙烯基三甲氧基硅烷替换为二甲基乙烯基硅氧烷。The difference from Example 1 is that vinyltrimethoxysilane in step (4) is replaced by dimethylvinylsiloxane.
性能测试Performance Testing
分别测定实施例1-4、对比例1-2制得的产品的粘度、硬度、断裂伸长率、稳定性。The viscosity, hardness, elongation at break and stability of the products prepared in Examples 1-4 and Comparative Examples 1-2 were measured respectively.
粘度参考GB/T 10427-2008,采用旋转粘度计进行测试。The viscosity refers to GB/T 10427-2008, and is tested with a rotational viscometer.
硬度参考GB/T 531.1-2009,采用硬度计进行测试。The hardness refers to GB/T 531.1-2009, and the hardness tester is used for testing.
断裂伸长率参考GB/T 528-2009,采用万能材料试验机进行测试。The elongation at break refers to GB/T 528-2009, and is tested by a universal material testing machine.
稳定性测试方法为:分别测定各产品在常温放置12个月前后的断裂伸长率,计算出变化率,变化率=(初始断裂伸长率-常温放置12个月的断裂伸长率)/初始断裂伸长率×100%,变化率越低表明稳定性越好。The stability test method is: measure the elongation at break of each product before and after being placed at room temperature for 12 months, calculate the change rate, change rate = (initial elongation at break - elongation at break placed at room temperature for 12 months) / The initial elongation at break × 100%, the lower the change rate, the better the stability.
测试结果如表1所示:The test results are shown in Table 1:
表1Table 1
由表1可看出,本发明实施例1-4制得的低粘度烷氧基封端聚二甲基硅氧烷的粘度均较低,硬度、断裂伸长率、稳定性均较好。对比例1-2的部分步骤与实施例1不同,其中,对比例1的粘度和变化率均明显升高,说明含氢双封头对产品的粘度能起到较好的降低作用,对稳定性能起到较好的提高作用,而对比例2的硬度和断裂伸长率均明显下降,说明乙烯基三甲氧基硅烷对产品的硬度和断裂伸长率能起到较好的提高作用。It can be seen from Table 1 that the low-viscosity alkoxy-terminated polydimethylsiloxanes prepared in Examples 1-4 of the present invention have lower viscosity, better hardness, elongation at break and stability. Part of the steps in Comparative Examples 1-2 are different from those in Example 1. Among them, the viscosity and rate of change of Comparative Example 1 are significantly increased, indicating that the hydrogen-containing double-head can effectively reduce the viscosity of the product and stabilize the product. The performance plays a better role in improving, while the hardness and elongation at break of Comparative Example 2 are significantly decreased, indicating that vinyltrimethoxysilane can play a better role in improving the hardness and elongation at break of the product.
上述实施例仅例示性说明本发明的原理及其功效,而非用于限制本发明。任何熟悉此技术的人士皆可在不违背本发明的精神及范畴下,对上述实施例进行修饰或改变。因此,举凡所属技术领域中具有通常知识者在未脱离本发明所揭示的精神与技术思想下所完成的一切等效修饰或改变,仍应由本发明的权利要求所涵盖。The above-mentioned embodiments merely illustrate the principles and effects of the present invention, but are not intended to limit the present invention. Anyone skilled in the art can modify or change the above embodiments without departing from the spirit and scope of the present invention. Therefore, all equivalent modifications or changes made by those with ordinary knowledge in the technical field without departing from the spirit and technical idea disclosed in the present invention should still be covered by the claims of the present invention.
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