期刊文献+

本体聚合法制备高分子减阻剂的特性黏数研究 被引量:5

Intrinsic Viscosity of Polymer Drag Reducer Prepared by Bulk Polymerization
在线阅读 下载PDF
导出
摘要 采用本体聚合法,以TiCl_4/Al(i-Bu)_3为复合催化剂,α-烯烃为单体,合成了α-己烯/α-十二烯二元聚合物(简称高聚物),考察了反应条件对高聚物特性黏数的影响及高聚物共混对共混物特性黏数的影响。实验结果表明,在较佳的高聚物合成条件(主催化剂TiCl_4用量0.08 g、反应温度-5℃、V(α-己烯):V(α-十二烯)=1:3、助催化剂Al(i-Bu)_3用量0.10 mL、反应时间48 h)下,高聚物的特性黏数达到11.10 dL/g;加入少量二苯基二甲氧基硅烷可增大高聚物的特性黏数;共混物的特性黏数均大于单一高聚物的特性黏数;以TiCl_4/Al(Et)_3/Al(i-Bu)_3为复合催化剂时可提高高聚物的特性黏数。XRD和IR表征结果显示,合成的高聚物为结晶度较低的柔性α-烯烃聚合物。 A α-hexylene/α-dodecene copolymer was synthesized by bulk polymerization with TiCla/AI(i-Bu) 3 catalyst and α-olefin monomers. The effects of reaction conditions including catalyst dosage, V ( α-hexylene )/V ( α-dodecene ) ratio, polymer blending and reaction temperature on the intrinsic viscosity of the copolymer were investigated. The experimental results showed that the intrinsic viscosity of the copolymer could be up to 11.10 dL/g under the optimum conditions of catalyst TiCl4 0. 08 g, co-catalyst Al (i-Bu) 30. 10 mL, V(α-hexylene) : V(α-dodecene) 1 : 3, reaction temperature -5 ℃ and reaction time 48 h. The intrinsic viscosity can be improved by adding small amount of diphenyl dimethoxysilane; the intrinsic viscosity of the copolymer is higher than that of the single polymer; and TiCla/Al (Et) 3/Al (i-Bu) 3 composite catalyst can increase the intrinsic viscosity of the polymer. The XRD and IR experiments showed that the α-olefin polymer with low degree of crystallinity and flexibility was synthesized.
出处 《石油化工》 CAS CSCD 北大核心 2011年第2期198-202,共5页 Petrochemical Technology
基金 国家自然科学基金资助项目(20963010)
关键词 本体聚合法 Α-烯烃 二苯基二甲氧基硅烷 复合催化剂 原油减阻剂 bulk polymerization α-olefin diphenyl dimethoxysilane composite catalyst crude oil drag reducer
  • 相关文献

参考文献12

二级参考文献55

  • 1郑文,张玲,杨士林.油溶性减阻功能聚合物的研制[J].石油化工,1993,22(1):38-41. 被引量:12
  • 2米红宇,王吉德,李惠萍,奚惠明,买苏尔.米吉提,司马义.努尔拉.原油高效减阻剂的制备及其性能[J].精细石油化工,2005,22(2):12-15. 被引量:23
  • 3支俊格,刘安华,朱志国,吕晓村,范星河,陈小芳,宛新华,周其凤.一种手性甲壳型液晶高分子的稀溶液行为及链刚性[J].高分子学报,2005,15(5):774-778. 被引量:2
  • 4芦蓉,陈立滇.2-丙烯酰胺-2-甲基丙磺酸(AMPS)的应用[J].精细石油化工,1996,13(4):43-46. 被引量:19
  • 5Sellin R H J, Hoyt J W, Scrivener O. The effect of drag-reducing additives on liquid flows and their industrial applications Part 1: Basic aspects. J Hydraulic Res, 1982,20(1):29-68
  • 6Moussa T, Tiu C, Sridhar T, Effect of solvent on polymer degradation in turbulent flow. Journal of Non-Newtonian Fluid Mechanics, 1993, 48(3) :261-284
  • 7White D A. Prelimary experiments on polymer degradation in a turbulentshear field. Chem Eng Sci, 1970,25(8):1255- 1258
  • 8Fisher D, Rodriguez F. Degradation of drag reducing polymers. J Appl Polym Sci, 1971,15:2975-2985
  • 9Yu J F S, Zakin J L, Patierson J K. Mechanical degradation of high molecular weight polymers in dilute solution. Journal of Applied Polymer Science, 1979,23 : 2493-2512
  • 10Gampert B, Wagner P. The influence of molecular weight and molecular weight distribution on drag reduction and mechanical degradation in turbulent flows of highly dilute polymer solutions, in:Gampert B. Ed. The Influence of Polymer Additives onVelocity and Temperature Fields. New York: Springer-Verlag, 1985.71-85

共引文献65

同被引文献61

引证文献5

二级引证文献11

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部