华南师范大学学报(自然科学版)
華南師範大學學報(自然科學版)
화남사범대학학보(자연과학판)
JOURNAL OF SOUTH CHINA NORMAL UNIVERSITY (NATURAL SCIENCE EDITION)
2015年
1期
69-72
,共4页
王力%伊然%谢思%吴宏海%朱宏
王力%伊然%謝思%吳宏海%硃宏
왕력%이연%사사%오굉해%주굉
可聚合乳化剂%高固高羟基含量%核壳结构%苯丙微乳液
可聚閤乳化劑%高固高羥基含量%覈殼結構%苯丙微乳液
가취합유화제%고고고간기함량%핵각결구%분병미유액
polymerizable emulsifier%high solid hydroxyl content%core-shell structure%styrene-acrylic microemulsion
采用连续滴加预乳液的种子乳液聚合法,合成出固含量为42.76%、乳化剂质量分数为1%的具有核壳结构的苯乙烯丙烯酸酯微乳液.考察了乳化剂用量、羟基单体用量、甲基丙烯酸的用量等因素对乳液粒径及性能的影响.结果表明,聚合在相当于Winsor-I型的聚合体系中进行,由纯单体相(滴入的单体)和O/W微乳相构成,上层单体只起储存库的作用,它在缓慢的搅拌下扩散进入微乳相中.只要微乳液液面上补加的单体不扰动微乳液的平衡,就不会产生粗粒子.单体滴加时间控制在2 h,油酸钠∶OP-10=1∶1(质量比),NaHCO3占单体质量分数的0.15%,反应温度控制在78~82℃,可使聚合反应平稳进行.
採用連續滴加預乳液的種子乳液聚閤法,閤成齣固含量為42.76%、乳化劑質量分數為1%的具有覈殼結構的苯乙烯丙烯痠酯微乳液.攷察瞭乳化劑用量、羥基單體用量、甲基丙烯痠的用量等因素對乳液粒徑及性能的影響.結果錶明,聚閤在相噹于Winsor-I型的聚閤體繫中進行,由純單體相(滴入的單體)和O/W微乳相構成,上層單體隻起儲存庫的作用,它在緩慢的攪拌下擴散進入微乳相中.隻要微乳液液麵上補加的單體不擾動微乳液的平衡,就不會產生粗粒子.單體滴加時間控製在2 h,油痠鈉∶OP-10=1∶1(質量比),NaHCO3佔單體質量分數的0.15%,反應溫度控製在78~82℃,可使聚閤反應平穩進行.
채용련속적가예유액적충자유액취합법,합성출고함량위42.76%、유화제질량분수위1%적구유핵각결구적분을희병희산지미유액.고찰료유화제용량、간기단체용량、갑기병희산적용량등인소대유액립경급성능적영향.결과표명,취합재상당우Winsor-I형적취합체계중진행,유순단체상(적입적단체)화O/W미유상구성,상층단체지기저존고적작용,타재완만적교반하확산진입미유상중.지요미유액액면상보가적단체불우동미유액적평형,취불회산생조입자.단체적가시간공제재2 h,유산납∶OP-10=1∶1(질량비),NaHCO3점단체질량분수적0.15%,반응온도공제재78~82℃,가사취합반응평은진행.
The styrene-acrylic microemulsion with a core-shell structure having 42.76%solid content and 1%emul-sifier was synthesized by seed emulsion polymerization with the pre-emulsion continuously.The effects of dosage of e-mulsifier, hydroxyl monomer and methacrylic acid on the emulsion particle size and the properties of emulsion were investigated.Results showed that the polymerization was conducted in the system of equivalent Winsor-I type, which was composed of the pure monomer phase (monomer dropwise) and O/W microemulsion phase.The upper monomer only had the function of repository, which diffused into the microemulsion phase by slow stirring.Coarse particles would not form if the addition of the monomer did not disturb the balance of the microemulsion.The polymerization reaction could proceed smoothly with the following conditions:Monomer dropping time within 2 h, oil sodium∶OP-10=1∶1(mass ratio), NaHCO3 accounting for 0.15%of monomer mass fraction, reaction temperature at 78-82℃.