2004
DOI: 10.1016/j.polymer.2004.06.024
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Morphological, mechanical and gas-transport characteristics of crosslinked poly(propylene glycol): homopolymers, nanocomposites and blends

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Cited by 35 publications
(21 citation statements)
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“…Doucoure et al [19] had reported in-situ plasma polymerization of fluorinated monomers on mesoporous silica membranes. Patel et al [20,21] prepared cross-linked composite membranes of polyethylene glycol (PEG)/silica and poly (propylene glycol) (PPG)/silica by dispersing silica nanoparticles in diacrylate-terminated PEG and PPG, and subsequent radical polymerization initiated by 2,2'-azobisisobutyronitrile (AIBN). Nunes et al [22] synthesized the poly(ether imide) (PEI)/SiO 2 composite membranes by using in-situ polymerization.…”
Section: In-situ Polymerization Methodsmentioning
confidence: 99%
“…Doucoure et al [19] had reported in-situ plasma polymerization of fluorinated monomers on mesoporous silica membranes. Patel et al [20,21] prepared cross-linked composite membranes of polyethylene glycol (PEG)/silica and poly (propylene glycol) (PPG)/silica by dispersing silica nanoparticles in diacrylate-terminated PEG and PPG, and subsequent radical polymerization initiated by 2,2'-azobisisobutyronitrile (AIBN). Nunes et al [22] synthesized the poly(ether imide) (PEI)/SiO 2 composite membranes by using in-situ polymerization.…”
Section: In-situ Polymerization Methodsmentioning
confidence: 99%
“…As a result, the available vacant sites in polymer matrix are increased which accounts for the increase in the solvent uptake during swelling. [35][36][37][38] However, the observed decrease in crosslinking density may be attributed to the increase in exfoliated dispersion in the nanocomposites. 39 …”
Section: Limiting Oxygen Indexmentioning
confidence: 99%
“…However, the affinity of the membrane material for CO 2 must not be too high such that a strong bond is formed with CO 2 , or else the CO 2 flux will suffer detrimentally. Other rubbery polymers that may be of interest for CO 2 separation (reverse H 2 separation) include polyphosphazenes [55,56] and poly(ethylene glycol) [57][58][59], although, substantial work is required in this area before commercialisation can occur. A disadvantage of these membranes is that although they are more permeable to condensable gases such as CO 2 or H 2 S at lower temperatures (25 1C), with increasing temperature H 2 becomes more mobile and these membranes may also allow H 2 to migrate through [60].…”
Section: Article In Pressmentioning
confidence: 99%