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1.昆明理工大学化学工程学院,云南 昆明 650500
2.昆明理工大学理学院,云南 昆明 650500
Received:10 September 2018,
Revised:2018-12-06,
Online First:24 July 2026,
Published:05 March 2019
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周强, 郝军正, 祝琳华, 王红, 司甜, 何艳萍, 孙彦琳. 泡沫相相分离制备多孔聚合物微球连续化工艺[J]. 化工学报, 2019, 70(3): 1208-1219
ZHOU Qiang, HAO Junzheng, ZHU Linhua, WANG Hong, SI Tian, HE Yanping, SUN Yanlin. Foam phase preparation of porous poly(methyl methacrylate-co-butyl acrylate) microspheres in continuous process[J]. CIESC Journal, 2019, 70(3): 1208-1219
周强, 郝军正, 祝琳华, 王红, 司甜, 何艳萍, 孙彦琳. 泡沫相相分离制备多孔聚合物微球连续化工艺[J]. 化工学报, 2019, 70(3): 1208-1219 DOI: 10.11949/j.issn.0438-1157.20181012.
ZHOU Qiang, HAO Junzheng, ZHU Linhua, WANG Hong, SI Tian, HE Yanping, SUN Yanlin. Foam phase preparation of porous poly(methyl methacrylate-co-butyl acrylate) microspheres in continuous process[J]. CIESC Journal, 2019, 70(3): 1208-1219 DOI: 10.11949/j.issn.0438-1157.20181012.
采用在泡沫相进行溶剂挥发的方法,连续、高效制备聚甲基丙烯酸甲酯-丙烯酸丁酯[P(MMA-BA)]共聚物多孔微球。采用自制的连续化反应装置,在一定搅拌速率和反应温度下,向反应器连续加料,在出口处连续收集溢出的泡沫并进行消泡、分散,再经洗涤、过滤、干燥得到多孔聚合物微球。重点研究了油相进料速率、反应温度、搅拌速率、聚乙烯醇用量(PVA浓度)对平均泡沫溢出速率、微球收率、微球粒径以及多孔形态的影响规律。结果表明:在反应温度为45℃,搅拌速率为500 r/min,油相溶液进料速率为30 g/min,PVA浓度为1.0%(质量),油相溶液中P(MMA-BA)∶二氯甲烷(DCM)∶正庚烷(HT)=10∶53∶6(质量比)的工艺条件下,聚合物微球的收率高达92%,平均粒径为130 μm,P(MMA-BA)微球球形饱满,呈多孔结构。
Porous polymeric microspheres have been widely used since their characteristics in the structure. However
the reported methods are less efficient
especially no continuous process was reported to prepare porous polymeric microspheres. Therefore
there is a need to develop a time-saving method with high yield for producing porous polymeric microspheres. This paper reports a continuous process to prepare porous polymeric microspheres
via
the solvent evaporation method in foam phase
being efficient and of high yield. Preparation of porous poly(methyl methacrylate-
co
-butyl acrylate) [P(MMA-BA)
]
microspheres was carried out in a customized continuous reaction device. At a certain stirring rate and reaction temperature
the oil phase and the aqueous phase were pumped continuously into the reactor. Foam phase gradually generated and flowed out from the outlet of the reactor. Porous P(MMA-BA) microspheres were obtained after collecting the bubble phase followed by defoaming
washing
filtration and drying. The average foam flow rate
the microspheres’ yield
the average particle size and the pore structure were investigated as a function of the experimental conditions including the feed rate of the oil phase
the reaction temperature
the stirring rate and the concentration of PVA. The results showed that the reaction temperature was 45℃
the stirring rate was 500 r/min
the oil phase solution feed rate was 30 g/min
the PVA concentration was 1.0% (mass)
and the oil phase solution P (MMA-BA): DCM∶HT is 10∶53∶6 respectively
the yield of the porous P(MMA-BA) microspheres was up to 92% and the average particle size is 130 µm. The temperature and the residual amount of the aqueous phase left in the customized continuous reaction device are critical for the foam behavior and the yield of the porous P(MMA-BA) microspheres. This work validates that the customized continuous reaction device is capable to produce porous polymeric microspheres continuously
based on the method to prepar
e porous polymeric microspheres
via
solvent evaporation method in foam phase
with improved efficiency and yield. In addition
the method reported in this work is able to use continuously on an industrial scale potentially.
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