[go: up one dir, main page]

CN103304818A - Preparation method of methyl phenyl silicone oil - Google Patents

Preparation method of methyl phenyl silicone oil Download PDF

Info

Publication number
CN103304818A
CN103304818A CN2013102609202A CN201310260920A CN103304818A CN 103304818 A CN103304818 A CN 103304818A CN 2013102609202 A CN2013102609202 A CN 2013102609202A CN 201310260920 A CN201310260920 A CN 201310260920A CN 103304818 A CN103304818 A CN 103304818A
Authority
CN
China
Prior art keywords
silicone oil
add
dimethyldichlorosilane
methyl phenyl
distilled 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.)
Granted
Application number
CN2013102609202A
Other languages
Chinese (zh)
Other versions
CN103304818B (en
Inventor
殷恒波
马克超
胡永明
毛雨林
王爱丽
冯永海
沈灵沁
谢文静
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu University
Original Assignee
Jiangsu University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jiangsu University filed Critical Jiangsu University
Priority to CN201310260920.2A priority Critical patent/CN103304818B/en
Publication of CN103304818A publication Critical patent/CN103304818A/en
Application granted granted Critical
Publication of CN103304818B publication Critical patent/CN103304818B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Silicon Polymers (AREA)

Abstract

本发明涉及一种甲基苯基硅油的制备方法,属于有机硅合成技术领域。该方法是将一定比例的二甲基二氯硅烷和二苯基二氯硅烷单体加入到二甲苯和丙酮的混合溶剂中混合均匀,采用逆水解法向其中滴加丙酮和水的混合水解液,滴加完毕后加入一定量的封端剂,在30℃下继续反应一段时间,水解结束。静置分层,分出下层酸水,上层水解物用热蒸馏水洗至中性,得到硅氧烷预聚物,向其中加入一定量的缩合催化剂进行缩合反应结束后,用热蒸馏水洗去催化剂至中性,然后在减压条件下蒸出溶剂二甲苯和低沸物,得到甲基苯基硅油产品。本发明制备的甲基苯基硅油为澄清半透明油状液体,产品均匀性较好,纯度高,制备工艺条件简单,溶剂可回收利用,易于工业化生产。

Figure 201310260920

The invention relates to a preparation method of methylphenyl silicone oil, which belongs to the technical field of organosilicon synthesis. The method is to add a certain proportion of dimethyldichlorosilane and diphenyldichlorosilane monomers into a mixed solvent of xylene and acetone and mix evenly, and then add a mixed hydrolyzate of acetone and water dropwise to it by reverse hydrolysis method, After the dropwise addition, a certain amount of end-capping agent was added, and the reaction was continued for a period of time at 30° C., and the hydrolysis was completed. Stand for stratification, separate the lower layer of acid water, and wash the upper layer of hydrolyzate with hot distilled water until neutral to obtain a siloxane prepolymer, add a certain amount of condensation catalyst to it for condensation reaction, wash off the catalyst with hot distilled water to neutrality, and then distill off the solvent xylene and low boilers under reduced pressure to obtain methyl phenyl silicone oil products. The methylphenyl silicone oil prepared by the invention is a clear translucent oily liquid, has good product uniformity, high purity, simple preparation process conditions, recyclable solvent and is easy for industrialized production.

Figure 201310260920

Description

一种甲基苯基硅油的制备方法A kind of preparation method of methylphenyl silicone oil

技术领域:Technical field:

本发明涉及硅油的制备方法,具体是指一种三甲基硅氧烷封端的二甲基二苯基硅油的制备方法,产品为澄清半透明油状液体,均匀性好,纯度高。 The invention relates to a method for preparing silicone oil, in particular to a method for preparing trimethylsiloxane-terminated dimethyldiphenyl silicone oil. The product is a clear translucent oily liquid with good uniformity and high purity.

背景技术:Background technique:

   硅油通常指室温下保持液体状态的线型聚硅氧烷,最常用的硅油有机基团全部为甲基,称为甲基硅油,而甲基苯基硅油是甲基硅油中部分甲基被苯基取代后的产物,具有优异的耐高低温性、润滑性和耐辐照性,是发展前景广阔的产品。 Silicone oil usually refers to a linear polysiloxane that maintains a liquid state at room temperature. The organic groups of the most commonly used silicone oil are all methyl, called methyl silicone oil, and methyl phenyl silicone oil is part of the methyl group in methyl silicone oil that is covered with benzene. The products substituted with radicals have excellent high and low temperature resistance, lubricity and radiation resistance, and are products with broad development prospects.

目前,关于甲基苯基硅油的制备方法较多,例如,专利CN 102070785A公布了一种以甲基苯基二氯硅烷水解物、二甲基二氯硅烷水解物、甲基苯基环硅氧烷为原料制备羟基封端聚甲基苯基硅氧烷的方法;专利CN 101851333A公布了一种以甲基苯基环硅氧烷、二甲基环硅氧烷、甲基氢环硅氧烷为原料,稀土超强酸为催化剂制备甲基苯基含氢硅油。上述方法主要以环硅氧烷为原料制备甲基苯基硅油,增加了产品制备的成本,并不有利于工业化生产。专利CN 102516546A公布了一种以甲基苯基二氯硅烷为原料,弱有机碱水溶液为缚酸剂制备低粘度甲基苯基羟基硅油,该方法虽然原料价廉,但加入了大量的弱有机碱,增加了工业化生产的成本。 At present, there are many preparation methods for methylphenyl silicone oil. For example, patent CN 102070785A discloses a method of using methylphenyldichlorosilane hydrolyzate, dimethyldichlorosilane hydrolyzate, methylphenylcyclosiloxane Alkane is the method for preparing hydroxyl-terminated polymethylphenylsiloxane as raw material; Patent CN 101851333A discloses a method of using methylphenylcyclosiloxane, dimethylcyclosiloxane, methylhydrogencyclosiloxane As raw material, rare earth super acid is used as catalyst to prepare methyl phenyl hydrogen-containing silicone oil. The above method mainly uses cyclosiloxane as a raw material to prepare methylphenyl silicone oil, which increases the cost of product preparation and is not conducive to industrial production. Patent CN 102516546A discloses a kind of using methylphenyl dichlorosilane as raw material and weak organic alkali aqueous solution as acid-binding agent to prepare low-viscosity methylphenyl hydroxy silicone oil. Although the raw material is cheap, a large amount of weak organic Alkali increases the cost of industrialized production.

发明内容:Invention content:

本发明提出了一种甲基苯基硅油的制备方法,具体是指一种三甲基硅氧烷封端的二甲基二苯基硅油的制备方法,该方法工艺简单、反应条件温和、原料易得、成本低、易于工业化生产。 The present invention proposes a method for preparing methylphenyl silicone oil, specifically a method for preparing trimethylsiloxane-terminated dimethyldiphenyl silicone oil. The method has simple process, mild reaction conditions, and easy raw materials. The invention has the advantages of low cost and easy industrial production.

本发明是通过下述技术方案得以实现的: The present invention is achieved through the following technical solutions:

一种甲基苯基硅油的制备方法,其特征是按下述步骤进行的: A preparation method of methyl phenyl silicone oil is characterized in that it is carried out in the following steps:

(1)在500 mL三口烧瓶中按每7.74~23.23 g二甲基二氯硅烷加入5.06~35.45 g二苯基二氯硅烷、80 mL二甲苯、50 mL丙酮,在30 ℃下搅拌混合均匀;用丙酮和蒸馏水配置水解液,丙酮和蒸馏水的用量为按每7.74~23.23g二甲基二氯硅烷和5.06~35.45 g二苯基二氯硅烷加入100 mL丙酮和57.6 g蒸馏水,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,滴加完毕后加入一定量的封端剂,在30 ℃下继续反应5 h,水解结束; (1) Add 5.06 to 35.45 g of diphenyldichlorosilane, 80 mL of xylene, and 50 mL of acetone for every 7.74 to 23.23 g of dimethyldichlorosilane in a 500 mL three-necked flask, and stir and mix evenly at 30 °C; Use acetone and distilled water to prepare the hydrolyzate. The dosage of acetone and distilled water is to add 100 mL of acetone and 57.6 g of dichlorosilane for every 7.74~23.23g of dimethyldichlorosilane and 5.06~35.45g of diphenyldichlorosilane, stir well, and use The constant pressure titration funnel was added drop by drop to the three-necked flask, and the dropping rate was controlled to keep 1d/2s. After the dropwise addition, a certain amount of end-capping agent was added, and the reaction was continued at 30°C for 5 h, and the hydrolysis was completed;

(2)静置分层,分出下层酸水,上层水解物用50~60 ℃的蒸馏水洗至中性,得到硅氧烷预聚物,然后在80~120 ℃下加入缩合催化剂进行缩合反应1~8 h,反应结束后,用50~60 ℃的蒸馏水洗去催化剂至中性,然后在130 ℃减压条件 (2) Stand for stratification, separate the lower layer of acid water, and wash the upper layer of hydrolyzate with distilled water at 50-60 °C until neutral to obtain a siloxane prepolymer, and then add a condensation catalyst at 80-120 °C for condensation reaction 1 to 8 hours, after the reaction is over, wash the catalyst with distilled water at 50 to 60 °C until neutral, and then under reduced pressure at 130 °C

下蒸出溶剂二甲苯和低沸物,得到甲基苯基硅油产品。 The solvent xylene and low boilers are distilled off to obtain methylphenyl silicone oil product.

其中步骤(1)中加入的二甲基二氯硅烷、二苯基二氯硅烷的量为:二甲基二氯硅烷和二苯基二氯硅烷的总摩尔量为0.2 mol,二甲基二氯硅烷和二苯基二氯硅烷的质量比优选18.07:15.19; Wherein the amount of dimethyl dichlorosilane and diphenyl dichlorosilane added in the step (1) is: the total molar weight of dimethyl dichlorosilane and diphenyl dichlorosilane is 0.2 mol, dimethyl dichlorosilane The mass ratio of chlorosilane and diphenyldichlorosilane is preferably 18.07:15.19;

其中步骤(1)中所述的封端剂为三甲基氯硅烷,加入量为:三甲基氯硅烷与二甲基二氯硅烷和二苯基二氯硅烷的总摩尔比为1:10~1:80,为0.2716~2.1728 g; Wherein the capping agent described in the step (1) is trimethylchlorosilane, and the addition amount is: the total molar ratio of trimethylchlorosilane to dimethyldichlorosilane and diphenyldichlorosilane is 1:10 ~1:80, 0.2716~2.1728 g;

其中步骤(2)中加入缩合催化剂进行缩合反应时,缩合催化剂加入量为二甲基二氯硅烷和二苯基二氯硅烷总质量的0.01% ~0.2%,为0.0133 g~0.2660 g; Wherein step (2) when adding a condensation catalyst to carry out the condensation reaction, the amount of the condensation catalyst added is 0.01% to 0.2% of the total mass of dimethyldichlorosilane and diphenyldichlorosilane, which is 0.0133 g to 0.2660 g;

其中步骤(2)中所述的缩合催化剂为25wt%乙醇钠的乙醇溶液; Wherein the condensation catalyst described in step (2) is the ethanolic solution of 25wt% sodium ethylate;

其中步骤(2)所述的催化剂缩合反应的最佳反应温度为100℃,最佳缩合反应时间为3h。 Wherein the optimal reaction temperature of the catalyst condensation reaction described in step (2) is 100° C., and the optimal condensation reaction time is 3 hours.

本发明的优点在于: The advantages of the present invention are:

1. 本发明采用的原料为氯硅烷单体,原料简单、可以由直接法生产、产量大、成本低、易得,使得甲基苯基硅油更加容易工业化生产,同时工艺简单、反应条件温和;溶剂二甲苯可以通过减压蒸馏回收再利用。 1. The raw material used in the present invention is chlorosilane monomer, which is simple, can be produced by direct method, has large output, low cost, and is easy to obtain, which makes industrial production of methylphenyl silicone oil easier, and at the same time, the process is simple and the reaction conditions are mild; The solvent xylene can be recovered and reused by vacuum distillation.

2. 本发明采用强碱乙醇钠为催化剂,用量少,能有效地催化硅氧烷预聚物缩合制备甲基苯基硅油。 2. The present invention uses a strong base, sodium ethoxide, as a catalyst with a small dosage, which can effectively catalyze the condensation of siloxane prepolymers to prepare methylphenyl silicone oil.

3. 本发明合成的硅油为澄清半透明油状液体,分子量分布小,均匀性好,纯度高。 3. The silicone oil synthesized by the present invention is a clear translucent oily liquid with small molecular weight distribution, good uniformity and high purity.

4. 本发明在氯硅烷水解时产生大量的废盐酸,可以与铝土矿混合,取上层清液进行加热蒸发得氯化铝晶体,用作净水剂,达到综合回收利用的效果,同时减少环境污染。 4. The present invention produces a large amount of waste hydrochloric acid during the hydrolysis of chlorosilane, which can be mixed with bauxite, and the supernatant liquid is heated and evaporated to obtain aluminum chloride crystals, which are used as water purifiers to achieve the effect of comprehensive recycling and reduce environmental pollution.

附图说明 Description of drawings

图1为Ph/R比值为0.1时所制备的甲基苯基硅油GPC图谱。 Figure 1 is the GPC spectrum of methylphenyl silicone oil prepared when the Ph/R ratio is 0.1.

图2为Ph/R比值为0.3时所制备的甲基苯基硅油红外光谱图。 Fig. 2 is the infrared spectrogram of methylphenyl silicone oil prepared when the Ph/R ratio is 0.3.

图3为Ph/R比值为0.3时所制备的甲基苯基硅油GPC图谱。 Figure 3 is the GPC spectrum of methylphenyl silicone oil prepared when the Ph/R ratio is 0.3.

具体实施方式:Detailed ways:

以下为本发明的较佳实施例,能够更好地理解本发明,但本发明的实施例不限于此,同时其所示数据不代表对本发明特征范围的限制。 The following are preferred embodiments of the present invention, which can better understand the present invention, but the embodiments of the present invention are not limited thereto, and the data shown therein do not represent limitations to the scope of the present invention.

实施例1 Example 1

Ph/R比值(摩尔比)为0.1。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和23.23 g二甲基二氯硅烷、5.06 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0570 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。其GPC图谱见图1。其GPC图谱呈单峰分散方式,硅油均匀性好,纯度较高,分子量分布小。 The Ph/R ratio (molar ratio) was 0.1. Add 80 mL of xylene, 50 mL of acetone, 23.23 g of dimethyldichlorosilane and 5.06 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5h, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0570 g of condensation catalyst sodium ethylate (0.05% of the total monomer mass) at 100 °C for condensation reaction for 3 h. After the reaction, wash the catalyst with 50-60 °C distilled water to neutrality, and then The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product. Its GPC spectrum is shown in Figure 1. Its GPC spectrum shows a single-peak dispersion mode, and the silicone oil has good uniformity, high purity and small molecular weight distribution.

实施例2 Example 2

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。其红外光谱图见图2,GPC图谱见图3。其红外光谱图中3051.6 cm-1和3071.1 cm-1吸收峰归属于苯基不饱和氢的伸缩振动吸收;在2962.2和2904.2处的吸收峰为CH3-Si中C-H伸缩振动峰;在1429.7 cm-1强吸收峰归属于Si-Ph中芳环的振动吸收峰;在1261.4处产生的尖锐的吸收峰是Si-CH3的吸收峰;在1000~1120 cm-1有一宽而强的吸收带归属于Si-O-Si的反对称伸缩振动。其GPC图谱呈单峰分散方式,硅油均匀性好,纯度较高,分子量分布小。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane and 15.19 g of diphenyldichlorosilane into a 500 mL three-necked flask, and stir and mix evenly at 30 °C; prepare a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping rate to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capped Chlorotrimethylsilane, continue to react at 30°C for 5h, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (0.05% of the total monomer mass) at 100 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product. Its infrared spectrogram is shown in Figure 2, and its GPC spectrum is shown in Figure 3. In its infrared spectrum, the absorption peaks at 3051.6 cm -1 and 3071.1 cm -1 belong to the stretching vibration absorption of phenyl unsaturated hydrogen; the absorption peaks at 2962.2 and 2904.2 are CH stretching vibration peaks in CH 3 -Si; at 1429.7 cm The strong absorption peak of -1 is attributed to the vibration absorption peak of the aromatic ring in Si-Ph; the sharp absorption peak at 1261.4 is the absorption peak of Si-CH 3 ; there is a broad and strong absorption band at 1000-1120 cm -1 Attributed to the antisymmetric stretching vibration of Si-O-Si. Its GPC spectrum shows a single-peak dispersion mode, and the silicone oil has good uniformity, high purity and small molecular weight distribution.

实施例3 Example 3

Ph/R比值(摩尔比)为0.7。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和7.74 g二甲基二氯硅烷、35.45 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0864 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到白色较软固体甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.7. Add 80 mL of xylene, 50 mL of acetone, 7.74 g of dimethyldichlorosilane, and 35.45 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0864 g of condensation catalyst sodium ethylate (0.05% of the total mass of the monomer) at 100 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a white soft methyl phenyl silicone oil product.

实施例4 Example 4

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入2.1728 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 2.1728 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (the mass is 0.05% of the total mass of the monomer) at 100 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product.

实施例5 Example 5

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.2716 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.2716 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (the mass is 0.05% of the total mass of the monomer) at 100 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product.

实施例6 Example 6

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应1 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (0.05% of the total mass of the monomer) at 100 °C for condensation reaction for 1 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product.

实施例7 Example 7

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应8 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到黄色半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (the mass is 0.05% of the total mass of the monomer) at 100 °C for condensation reaction for 8 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a yellow translucent liquid methyl phenyl silicone oil product.

实施例8 Example 8

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在80 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (the mass is 0.05% of the total mass of the monomer) at 80 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product.

实施例9 Example 9

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在120 ℃下加入0.0665 g缩合催化剂乙醇钠(质量为单体总质量0.05%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到黄色半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0665 g of condensation catalyst sodium ethylate (0.05% of the total mass of the monomer) at 120 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a yellow translucent liquid methyl phenyl silicone oil product.

实施例10 Example 10

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.0133 g缩合催化剂乙醇钠(质量为单体总质量0.01%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到澄清半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.0133 g of condensation catalyst sodium ethylate (0.01% of the total mass of the monomer) at 100 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a clear translucent liquid methyl phenyl silicone oil product.

实施例11 Example 11

Ph/R比值(摩尔比)为0.3。在500 mL三口烧瓶中加入80 mL二甲苯、50 mL丙酮和18.07 g二甲基二氯硅烷、15.19 g二苯基二氯硅烷,在30 ℃下搅拌混合均匀;配置一定比例的水解液,其中丙酮100 mL和蒸馏水57.6 g,搅拌均匀,用恒压滴定漏斗向三口烧瓶中逐滴滴加,控制滴加速度保持1d/2s,总滴定时间为3 h左右,滴加完毕后加入0.5432 g封端剂三甲基氯硅烷,在30 ℃下继续反应5h,水解结束;静置分层,分出下层酸水,上层水解物用50~60 ℃蒸馏水洗至中性,得到硅氧烷预聚物,然后在100 ℃下加入0.2660 g缩合催化剂乙醇钠(质量为单体总质量0.2%)进行缩合反应3 h,反应结束后,用50~60 ℃蒸馏水洗去催化剂至中性,然后在130 ℃减压条件下蒸出溶剂二甲苯和低沸物,得到黄色半透明液态甲基苯基硅油产品。 The Ph/R ratio (molar ratio) was 0.3. Add 80 mL of xylene, 50 mL of acetone, 18.07 g of dimethyldichlorosilane, and 15.19 g of diphenyldichlorosilane into a 500 mL three-neck flask, stir and mix evenly at 30 °C; configure a certain proportion of hydrolyzate, of which Acetone 100 mL and distilled water 57.6 g, stir evenly, add drop by drop to the three-necked flask with a constant pressure titration funnel, control the dropping speed to keep 1d/2s, the total titration time is about 3 h, add 0.5432 g capping after the dropwise addition Chlorotrimethylsilane, continue to react at 30°C for 5 hours, and the hydrolysis is completed; stand for stratification, separate the lower layer of acid water, wash the upper layer of hydrolyzate with distilled water at 50-60°C until neutral, and obtain a siloxane prepolymer , and then add 0.2660 g of condensation catalyst sodium ethylate (the mass is 0.2% of the total mass of the monomer) at 100 °C for condensation reaction for 3 h. The solvent xylene and low boilers were distilled off under reduced pressure to obtain a yellow translucent liquid methyl phenyl silicone oil product.

Claims (6)

1. the preparation method of a methyl phenyl silicone oil, carry out in the steps below:
(1) in there-necked flask, adds 5.06~35.45 g diphenyl dichlorosilanes, 80 mL dimethylbenzene, 50 mL acetone by per 7.74 ~ 23.23 g dimethyldichlorosilane(DMCS)s, under 30 ℃, mix; With acetone and distilled water configuration hydrolyzed solution, the consumption of acetone and distilled water is for to add 100 mL acetone and 57.6 g distilled water by per 7.74 ~ 23.23g dimethyldichlorosilane(DMCS) and 5.06~35.45 g diphenyl dichlorosilanes, stir, dropwise drip in there-necked flask with constant voltage titration funnel, the control rate of addition keeps 1d/2s, dropwise a certain amount of end-capping reagent of rear adding, at 30 ℃ of lower reaction 5 h that continue, hydrolysis finishes;
(2) standing demix, tell lower floor's sour water, the upper strata hydrolyzate is washed till neutrality with 50~60 ℃ distilled water, obtain siloxane prepolymer, then carry out condensation reaction 1~8 h at 80~120 ℃ of lower condensation catalysts that add, after reaction finishes, extremely neutral with 50~60 ℃ distilled water flush away catalyzer, then 130 ℃ of reduced pressure
Under steam solvent xylene and low-boiling-point substance, obtain the methyl phenyl silicone oil product.
2. the preparation method of methyl phenyl silicone oil according to claim 1, it is characterized in that, the dimethyldichlorosilane(DMCS) that wherein adds in the step (1), the amount of diphenyl dichlorosilane are: the integral molar quantity of dimethyldichlorosilane(DMCS) and diphenyl dichlorosilane is 0.2 mol, and the mass ratio of dimethyldichlorosilane(DMCS) and diphenyl dichlorosilane is 18.07:15.19.
3. the preparation method of methyl phenyl silicone oil according to claim 1, it is characterized in that, wherein the end-capping reagent described in the step (1) is trimethylchlorosilane, add-on is: total mol ratio of trimethylchlorosilane and dimethyldichlorosilane(DMCS) and diphenyl dichlorosilane is 1:10~1:80, is 0.2716~2.1728 g.
4. the preparation method of methyl phenyl silicone oil according to claim 1, it is characterized in that, when wherein the adding condensation catalyst carries out condensation reaction in the step (2), the condensation catalyst add-on is 0.01% ~ 0.2% of dimethyldichlorosilane(DMCS) and diphenyl dichlorosilane total mass, is 0.0133 g~0.2660 g.
5. the preparation method of methyl phenyl silicone oil according to claim 1 is characterized in that, wherein the condensation catalyst described in the step (2) is the ethanolic soln of 25wt% sodium ethylate.
6. the preparation method of methyl phenyl silicone oil according to claim 1 is characterized in that, the temperature of reaction of the described catalyzer condensation reaction of step (2) is 100 ℃, and condensation reaction time is 3h.
CN201310260920.2A 2013-06-26 2013-06-26 A kind of preparation method of methyl phenyl silicone oil Expired - Fee Related CN103304818B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310260920.2A CN103304818B (en) 2013-06-26 2013-06-26 A kind of preparation method of methyl phenyl silicone oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310260920.2A CN103304818B (en) 2013-06-26 2013-06-26 A kind of preparation method of methyl phenyl silicone oil

Publications (2)

Publication Number Publication Date
CN103304818A true CN103304818A (en) 2013-09-18
CN103304818B CN103304818B (en) 2015-09-02

Family

ID=49130566

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310260920.2A Expired - Fee Related CN103304818B (en) 2013-06-26 2013-06-26 A kind of preparation method of methyl phenyl silicone oil

Country Status (1)

Country Link
CN (1) CN103304818B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108329475A (en) * 2018-01-30 2018-07-27 广东省石油与精细化工研究院 A kind of synthetic method of methyl phenyl silicone oil
CN110669221A (en) * 2019-10-31 2020-01-10 周民主 Hydrolysis method of high-boiling silicone oil
CN111534222A (en) * 2020-06-08 2020-08-14 无锡米克新材料有限公司 Organopolysiloxane rubber protective coating paint
CN116162245A (en) * 2022-12-29 2023-05-26 广州回天新材料有限公司 A kind of high boiling silicone oil and its preparation method and application
CN118580496A (en) * 2024-06-26 2024-09-03 新亚强硅化学股份有限公司 A method and equipment for preparing methylphenyl silicone oil

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106893618A (en) * 2017-02-08 2017-06-27 江苏大学 A kind of composite titan-based grease preparation method based on PSI

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3706775A (en) * 1970-12-17 1972-12-19 Wacker Chemie Gmbh Method of preparing high molecular weight linear organopolysiloxanes
GB1513310A (en) * 1974-09-16 1978-06-07 Gen Electric Organopolysiloxanes
US4390651A (en) * 1974-09-16 1983-06-28 General Electric Company Phenyl-containing organopolysiloxanes
CN1037158A (en) * 1988-12-12 1989-11-15 营口市熊岳制药厂 Preparation techlonogy for polydipheny dimethyl linear siloxane
CN1944492A (en) * 2005-10-04 2007-04-11 瓦克化学有限公司 Method for the preparation of organopolysiloxanes
CN102585226A (en) * 2012-02-13 2012-07-18 江苏大学 Preparation method for thermoset high temperature resistant methyl phenyl silicone resin

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3706775A (en) * 1970-12-17 1972-12-19 Wacker Chemie Gmbh Method of preparing high molecular weight linear organopolysiloxanes
GB1513310A (en) * 1974-09-16 1978-06-07 Gen Electric Organopolysiloxanes
US4390651A (en) * 1974-09-16 1983-06-28 General Electric Company Phenyl-containing organopolysiloxanes
CN1037158A (en) * 1988-12-12 1989-11-15 营口市熊岳制药厂 Preparation techlonogy for polydipheny dimethyl linear siloxane
CN1944492A (en) * 2005-10-04 2007-04-11 瓦克化学有限公司 Method for the preparation of organopolysiloxanes
CN102585226A (en) * 2012-02-13 2012-07-18 江苏大学 Preparation method for thermoset high temperature resistant methyl phenyl silicone resin

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王欣欣: "高粘度二甲基二苯基室温硫化硅橡胶的制备", 《有机硅材料及应用》, 22 November 1996 (1996-11-22), pages 14 - 17 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108329475A (en) * 2018-01-30 2018-07-27 广东省石油与精细化工研究院 A kind of synthetic method of methyl phenyl silicone oil
CN110669221A (en) * 2019-10-31 2020-01-10 周民主 Hydrolysis method of high-boiling silicone oil
CN111534222A (en) * 2020-06-08 2020-08-14 无锡米克新材料有限公司 Organopolysiloxane rubber protective coating paint
CN116162245A (en) * 2022-12-29 2023-05-26 广州回天新材料有限公司 A kind of high boiling silicone oil and its preparation method and application
CN118580496A (en) * 2024-06-26 2024-09-03 新亚强硅化学股份有限公司 A method and equipment for preparing methylphenyl silicone oil
CN118580496B (en) * 2024-06-26 2025-04-08 新亚强硅化学股份有限公司 Preparation method and equipment of methylphenyl silicone oil

Also Published As

Publication number Publication date
CN103304818B (en) 2015-09-02

Similar Documents

Publication Publication Date Title
CN103304818B (en) A kind of preparation method of methyl phenyl silicone oil
CN101717512B (en) A kind of preparation method of methylphenyl vinyl silicone resin
CN103012798B (en) Preparation method of methyl phenyl vinyl silicone resin
CN101906116B (en) Synthetic method of cagelike oct-polysilsesquioxane with same or different functional groups or non-functional groups
CN103408759B (en) A kind of preparation method of methyl phenyl silicone oil with high refractive index
CN102898649B (en) Refractive index-adjustable MDT silicone resin and preparation method thereof
CN106146850A (en) A kind of additional organosilicon impregnating resin viscosifier and preparation method thereof
CN101613476B (en) Silicon-hydrogen bond containing hyperbranched polyorganosiloxane and preparation method thereof
CN105085923B (en) A kind of Vinylphenyl silicon resin and preparation method thereof of solventless method synthesis
CN106478951A (en) A kind of preparation method of LED packaging plastic methyl and phenyl hydrogen-containing silicon oil
CN102268219A (en) Preparation method of solvent-free type organosilicon high-temperature-resistant paint
CN101781328A (en) Preparation method of cyclosiloxane
CN104558611B (en) A kind of MDTQ silicones and its preparation method and application
CN102634026A (en) Hydrogen-based silicone resin containing trifunctional group chain element and preparation method thereof
CN101768273B (en) Method for preparing multifunctional or non-functional terminal polysiloxane by ring-opening polymerization of cyclosiloxane
CN103834178B (en) Organic silicon resin as well as preparation method and application thereof
CN101298498A (en) Alkoxy terminated linear polysiloxane coupling agent and its synthesis method
CN101899156B (en) Preparation method of multichain trapezoidal polyalkyl silsesquioxane
CN101074284A (en) Production of polymethylphenylsilixane containing trifunctional phenyl-silox-chain
CN101230073B (en) Method for preparing phenyl-containing mixed cyclic siloxane
CN103204994B (en) Preparation method of phenyl silicon resin
CN102491991B (en) Organic silicon coupling agent containing beta-dicarbonyl and preparation method thereof
CN103588974B (en) The synthetic method of epoxy-modified polysiloxane flax soft finishing agent
CN104672274B (en) Contain a variety of functional group's polyhedral oligomeric silsesquioxanes and its synthetic method and application
CN103059301B (en) Phenyl hydrogen-containing reticular silicon resin for LED packaging and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150902

Termination date: 20160626

CF01 Termination of patent right due to non-payment of annual fee