2019
DOI: 10.3390/polym11020246
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Phase Behavior of a Carbon Dioxide/Methyl Trimethoxy Silane/Polystyrene Ternary System

Abstract: Recently, polymeric foams filled with a silica aerogel have been developed. The phase behavior of CO2/silicon alkoxide binary systems and CO2/silicon alkoxide/polymer ternary systems is an important factor that affects the design of novel processes. The phase behavior of a carbon dioxide (CO2)/methyl trimethoxy silane (MTMS)/polystyrene (PS) ternary system was measured using a synthetic method involving the observation of the bubble and cloud point. The phase boundaries were measured at temperatures ranging fr… Show more

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Cited by 4 publications
(2 citation statements)
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References 29 publications
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“…This solubility parameter can be determined experimentally or calculated based on the molecular structure, i.e., by the method reported by Fedors . ShellSolTD is a mixture of alkanes, and therefore, ShellSolTD was replaced by heptane, for which δ = 15.2 J 1/2 m –3/2 , and the heptane/toluene ratio was adjusted to vary the δ value between 15.2 and 18.2 J 1/2 m –3/2 (i.e., the δ value of toluene). , The calculated δ values of VPE (δ = 19.0 J 1/2 m –3/2 ) and of pVPE (δ = 21.1 J 1/2 m –3/2 ) are higher than those of styrene (17.8 J 1/2 m –3/2 ) and PS (δ = 17.4–19.0 J 1/2 m –3/2 ); , thus, the δ of a suitable porogen mixture (δ mix ) is also expected to be higher than the δ mix of the porogen used for the suspension polymerization of PS. Volumetric mixtures of 75:25 and 50:50 heptane and toluene with δ mix values of 15.6 and 16.9 J 1/2 m –3/2 , respectively, did dissolve VPE and resulted in the formation polymeric beads (Table , entries 1 and 2).…”
Section: Resultsmentioning
confidence: 99%
“…This solubility parameter can be determined experimentally or calculated based on the molecular structure, i.e., by the method reported by Fedors . ShellSolTD is a mixture of alkanes, and therefore, ShellSolTD was replaced by heptane, for which δ = 15.2 J 1/2 m –3/2 , and the heptane/toluene ratio was adjusted to vary the δ value between 15.2 and 18.2 J 1/2 m –3/2 (i.e., the δ value of toluene). , The calculated δ values of VPE (δ = 19.0 J 1/2 m –3/2 ) and of pVPE (δ = 21.1 J 1/2 m –3/2 ) are higher than those of styrene (17.8 J 1/2 m –3/2 ) and PS (δ = 17.4–19.0 J 1/2 m –3/2 ); , thus, the δ of a suitable porogen mixture (δ mix ) is also expected to be higher than the δ mix of the porogen used for the suspension polymerization of PS. Volumetric mixtures of 75:25 and 50:50 heptane and toluene with δ mix values of 15.6 and 16.9 J 1/2 m –3/2 , respectively, did dissolve VPE and resulted in the formation polymeric beads (Table , entries 1 and 2).…”
Section: Resultsmentioning
confidence: 99%
“…[30,31] For the preparation of porous particles using a non-solvent, a porogen is needed with a δ-value close to that of the monomer to ensure its dissolution, and different (preferable lower) than that of the resulting polymer, resulting in its precipitation. The δ-values of vinylindanone and poly-vinylindanone (pVI), as calculated based on the method reported by Fedors, [31] are much larger that the δ-values of styrene and polystyrene (20.5 and 22.9 vs 17.8 and 17.4-19.0 J 1/2 m −3/2 , respectively see supporting information section 3 [30,32] ). The porogen mixture used for the preparation of porous polystyrene particles has a delta-value (δ mix ) of 15.2 J 1/2 m −3/2 , which is lower than the δ-values of both styrene and polystyrene (lower by 2.6 and 2.2-3.8 J 1/2 m −3/2 , respectively).…”
Section: Polyvinylindanone Synthesis and Optimizationmentioning
confidence: 99%