CN103304818A - Preparation method of methyl phenyl silicone oil - Google Patents
Preparation method of methyl phenyl silicone oil Download PDFInfo
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- 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
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- dimethyldichlorosilane
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- 229920003216 poly(methylphenylsiloxane) Polymers 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000012153 distilled water Substances 0.000 claims abstract description 34
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000008096 xylene Substances 0.000 claims abstract description 28
- LIKFHECYJZWXFJ-UHFFFAOYSA-N dimethyldichlorosilane Chemical compound C[Si](C)(Cl)Cl LIKFHECYJZWXFJ-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000003054 catalyst Substances 0.000 claims abstract description 26
- OSXYHAQZDCICNX-UHFFFAOYSA-N dichloro(diphenyl)silane Chemical compound C=1C=CC=CC=1[Si](Cl)(Cl)C1=CC=CC=C1 OSXYHAQZDCICNX-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000009833 condensation Methods 0.000 claims abstract description 21
- 230000005494 condensation Effects 0.000 claims abstract description 21
- 238000006482 condensation reaction Methods 0.000 claims abstract description 20
- 230000007062 hydrolysis Effects 0.000 claims abstract description 16
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 16
- 239000002904 solvent Substances 0.000 claims abstract description 16
- KPUWHANPEXNPJT-UHFFFAOYSA-N disiloxane Chemical class [SiH3]O[SiH3] KPUWHANPEXNPJT-UHFFFAOYSA-N 0.000 claims abstract description 15
- 230000007935 neutral effect Effects 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims abstract description 10
- IJOOHPMOJXWVHK-UHFFFAOYSA-N chlorotrimethylsilane Chemical compound C[Si](C)(C)Cl IJOOHPMOJXWVHK-UHFFFAOYSA-N 0.000 claims description 30
- 238000003756 stirring Methods 0.000 claims description 25
- 238000004448 titration Methods 0.000 claims description 24
- QDRKDTQENPPHOJ-UHFFFAOYSA-N sodium ethoxide Chemical compound [Na+].CC[O-] QDRKDTQENPPHOJ-UHFFFAOYSA-N 0.000 claims description 14
- 239000005051 trimethylchlorosilane Substances 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 2
- QABCGOSYZHCPGN-UHFFFAOYSA-N chloro(dimethyl)silicon Chemical compound C[Si](C)Cl QABCGOSYZHCPGN-UHFFFAOYSA-N 0.000 claims 7
- 239000003153 chemical reaction reagent Substances 0.000 claims 2
- 239000000126 substance Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 15
- 239000002253 acid Substances 0.000 abstract description 14
- 239000000203 mixture Substances 0.000 abstract description 13
- 239000000178 monomer Substances 0.000 abstract description 13
- 238000013517 stratification Methods 0.000 abstract description 13
- 239000003795 chemical substances by application Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 239000012046 mixed solvent Substances 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 16
- 229920002545 silicone oil Polymers 0.000 description 10
- 238000010521 absorption reaction Methods 0.000 description 8
- 239000002994 raw material Substances 0.000 description 7
- 238000001228 spectrum Methods 0.000 description 6
- -1 polysiloxane Polymers 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000005046 Chlorosilane Substances 0.000 description 3
- KOPOQZFJUQMUML-UHFFFAOYSA-N chlorosilane Chemical compound Cl[SiH3] KOPOQZFJUQMUML-UHFFFAOYSA-N 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- GNEPOXWQWFSSOU-UHFFFAOYSA-N dichloro-methyl-phenylsilane Chemical compound C[Si](Cl)(Cl)C1=CC=CC=C1 GNEPOXWQWFSSOU-UHFFFAOYSA-N 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 229910002808 Si–O–Si Inorganic materials 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- MROCJMGDEKINLD-UHFFFAOYSA-N dichlorosilane Chemical compound Cl[SiH2]Cl MROCJMGDEKINLD-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 229920001921 poly-methyl-phenyl-siloxane Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000003930 superacid Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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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。
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.
Description
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
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
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
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
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
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
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
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
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
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
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
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
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