应用化学 ›› 2015, Vol. 32 ›› Issue (5): 527-534.DOI: 10.11944/j.issn.1000-0518.2015.05.140326

• 研究论文 • 上一篇    下一篇

线型二甲基硅氧烷低聚物的制备

曹都a,夏勇a,姚洪涛a,祁争健a*(),孙宇b,李丰富b   

  1. a东南大学化学化工学院 南京 211189
    b
    江苏美思德化学股份有限公司 南京 210046
  • 收稿日期:2014-09-19 修回日期:2014-12-04 接受日期:2015-01-28 出版日期:2015-05-05 发布日期:2015-05-05
  • 通讯作者: 祁争健
  • 基金资助:
    江苏省科技支撑项目(工业支撑BE 2012810);2013年普通高校研究生科研创新计划项目基金(CXLX13_106)

Synthesis of Linear Oligomer of Dimethyltetrasiloxane

CAO Dua, XIA Yonga, YAO Hongtaoa, QI Zhengjiana, *, SUN Yub, LI Fengfub   

  1. aCollege of Chemistry and Chemical Engineering, Southeast University, Nanjing 211189, China
    bJiangsu Maysta Chemical Co. Ltd., Nanjing 210046, China
  • Received:2014-09-19 Revised:2014-12-04 Accepted:2015-01-28 Published:2015-05-05 Online:2015-05-05
  • Contact: QI Zhengjian
  • Supported by:
    Supported by Jiangsu Province Science and Technology Support Program(No;BE 2012810), the Fundamental Research Funds for the Central Universities(No;CXLX13_106)

摘要:

以八甲基环四硅氧烷(D4)、六甲基二硅氧烷(MM)为原料, 采用固体超强酸(SA)TiO2/SO42-为催化剂合成线型二甲基硅氧烷四聚体(MD4M), 通过均匀设计实验和单因素实验分别研究了反应时间、反应温度、相对分子质量调节剂MM量和催化剂添加量对反应转化率和MD4M含量的影响, 结果表明, 当D4与MM的摩尔配比为0.75:1, 反应温度为100 ℃, 反应时间为7 h, 催化剂(SA)用量为反应物总质量的2%时, D4开环聚合制备线型二甲基硅氧烷低聚物的反应转化率为87%, 其中MD4M的收率为16.8%, 较硫酸催化体系提高了1.6%, 催化剂SA循环套用3次以上, 催化活性基本不变, 采用准均相体系建立了固体超强酸非均相催化D4开环聚合的宏观动力学模型。

 

关键词: 固体超强酸, 二甲基硅氧烷低聚物, 动力学

Abstract:

Linear dimethyltetrasiloxane(MD4M) was synthesized using octamethylcyclotetrasiloxane(D4) and hexamethyldisiloxane(MM) as raw materials and solid super acid(SA) TiO2/SO42- as catalyst. The influence of reaction time, reaction temperature, amount of relative molecular mass modifier(MM) and catalyst dosage on the degree of polymerization and the content of the product was studied by uniform design experiments and single factor experiments. Experiment results showed that the optimum reaction conditions are as follows:the molar ratio of octamethylcyclotetrasiloxane to hexamethyldisiloxane) is 0.75:1, the catalyst loading is 2%(mass fraction) of the total reactants, the reaction temperature is 100 ℃ and the reaction time is 7 h. The reaction conversion is 87% and the yield of MD4M is 16.8% which is 1.6% more than the sulfuric acid system. The catalyst(SA) can be recycled more than 3 times without the loss of its catalytic activity. The macro-kinetics model of the ring-opening polymerization of D4 with solid super acid as the heterogeneous catalyst was also created using the quasi-homogeneous system.

Key words: solid super acid, dimethyltetradesiloxane, dynamics

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