石油化工技术与经济
石油化工技術與經濟
석유화공기술여경제
TECHNO-ECONOMICS IN PETROCHEMICALS
2011年
3期
31-34
,共4页
陈金泉%谢家明%周立武%姚臻%曹堃
陳金泉%謝傢明%週立武%姚臻%曹堃
진금천%사가명%주립무%요진%조곤
双环戊二烯%苯乙烯%共聚%开环移位聚合
雙環戊二烯%苯乙烯%共聚%開環移位聚閤
쌍배무이희%분을희%공취%개배이위취합
DCPD%styrene%polymerization%ROMP
采用Grubbs催化剂进行双环戊二烯开环移位聚合,重点考察了本体聚合及双环戊二烯与苯乙烯共聚的影响因素,并利用红外光谱和差示扫描量热仪对产物的结构与性能进行了表征。结果表明,对于双环戊二烯本体聚合及双环戊二烯-苯乙烯共聚合体系,随着聚合温度的升高,反应速度增加,凝胶时间变短,但最终单体转化率基本不变;随着催化剂浓度的降低,体系凝胶时间延长。双环戊二烯与苯乙烯的配比对凝胶时间及转化率影响不大,但过量苯乙烯的引入会导致产物玻璃化温度的下降。
採用Grubbs催化劑進行雙環戊二烯開環移位聚閤,重點攷察瞭本體聚閤及雙環戊二烯與苯乙烯共聚的影響因素,併利用紅外光譜和差示掃描量熱儀對產物的結構與性能進行瞭錶徵。結果錶明,對于雙環戊二烯本體聚閤及雙環戊二烯-苯乙烯共聚閤體繫,隨著聚閤溫度的升高,反應速度增加,凝膠時間變短,但最終單體轉化率基本不變;隨著催化劑濃度的降低,體繫凝膠時間延長。雙環戊二烯與苯乙烯的配比對凝膠時間及轉化率影響不大,但過量苯乙烯的引入會導緻產物玻璃化溫度的下降。
채용Grubbs최화제진행쌍배무이희개배이위취합,중점고찰료본체취합급쌍배무이희여분을희공취적영향인소,병이용홍외광보화차시소묘량열의대산물적결구여성능진행료표정。결과표명,대우쌍배무이희본체취합급쌍배무이희-분을희공취합체계,수착취합온도적승고,반응속도증가,응효시간변단,단최종단체전화솔기본불변;수착최화제농도적강저,체계응효시간연장。쌍배무이희여분을희적배비대응효시간급전화솔영향불대,단과량분을희적인입회도치산물파리화온도적하강。
Ring- opening Metathesis Polymerization (ROMP) for dicyclopentadiene (DCPD) was made with Grubbs catalyst, and the affecting factors for mass polymerization and copolymerization of DCPD and styrene were analyzed. The structure and performance of the resultants of reaction were characterized with infrared spectrum and DSC. Result showed that for the DCPD mass polymerization and copolymerization of DCPD and styrene system, with the rising of reaction temperature, the reaction velocity raised, and the gelation time shortened, but the monomer conversion rate kept unchanged ; and with the decreasing of catalyst concentration, the gelation time for the system was prolonged. The ratio between DCPD and styrene has little effects on the gelation time and conversion rate, but overfeeding of styrene may cause drop of vitrification temperature for resultants.