2000
DOI: 10.1002/(sici)1521-3935(20000301)201:6<662::aid-macp662>3.0.co;2-1
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N-tert-Butyl-1-diethylphosphono-2,2-dimethylpropyl nitroxide as counter radical in the controlled free radical polymerization of styrene: kinetic aspects

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Cited by 52 publications
(22 citation statements)
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References 26 publications
(44 reference statements)
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“…This nitroxide is efficient with styrenic monomers at relatively high temperatures ( T = 123–135 °C). More recently, an important breakthrough has been the discovery of efficient acyclic nitroxides for NMP such as N ‐ tert ‐butyl‐ N ‐[1‐diethylphosphono‐(2,2‐dimethylpropyl)] nitroxide (SG1),30–33 and N ‐ tert ‐butyl‐ N ‐[1‐phenyl‐2‐(methylpropyl)] nitroxide (TIPNO), (Scheme ) 9, 34–38. This last generation of nitroxides is particularly well‐suited for the polymerization of styrenics,30, 36 alkyl acrylates,30, 36 methyl methacrylate (via a copolymerization approach),36, 39, 40 acrylic acid,41 acrylamides,42, 43 and dienes 34.…”
Section: Living/controlled Radical Polymerization (Lrp)mentioning
confidence: 99%
“…This nitroxide is efficient with styrenic monomers at relatively high temperatures ( T = 123–135 °C). More recently, an important breakthrough has been the discovery of efficient acyclic nitroxides for NMP such as N ‐ tert ‐butyl‐ N ‐[1‐diethylphosphono‐(2,2‐dimethylpropyl)] nitroxide (SG1),30–33 and N ‐ tert ‐butyl‐ N ‐[1‐phenyl‐2‐(methylpropyl)] nitroxide (TIPNO), (Scheme ) 9, 34–38. This last generation of nitroxides is particularly well‐suited for the polymerization of styrenics,30, 36 alkyl acrylates,30, 36 methyl methacrylate (via a copolymerization approach),36, 39, 40 acrylic acid,41 acrylamides,42, 43 and dienes 34.…”
Section: Living/controlled Radical Polymerization (Lrp)mentioning
confidence: 99%
“…In this scope, the initiator was prepared by trapping MAMA on the CC double bond of the n ‐butyl acrylate as a model initiator. Moreover, according to previous studies,38–40 we chose a [SG1]/[alkoxyamine] = 0.05 molar ratio.…”
Section: Resultsmentioning
confidence: 99%
“…In the present case, k pbutyl acrylate (88 000 L · mol −1 · s −1 , at 120 °C)48 is higher than k pstyrene (2 000 L · mol −1 · s −1 , at 120 °C) 49. The respective value of K and r for S and n ‐BuA are K styrene = 1.9.10 −8 mol · L −1 at 125 °C,39 K butyl acrylate = 1.2 · 10 −10 mol · L −1 at 125 °C50 and r styrene = 0.74, r butyl acrylate = 0.29 51. The high k p,butyl acrylate was counterbalanced by an increase of the 〈 K 〉 related to the high value of K styrene , the difference in the monomer reactivity ratio and the low k p,styrene .…”
Section: Resultsmentioning
confidence: 99%
“…The general characteristics of ATRP described in Sec. 3-15b apply to NMP, that is, reaction variables control polymerization rate, molecular weight, and PDI in the same way [Ananchenko and Fischer, 2001;Greszta and Matyjaszewski, 1996;Lacroix-Desmazes et al, 2000Lutz et al, 2001;Yoshikawa et al, 2002]. NMP with TEMPO generally requires higher temperatures (125-145 C) and longer reaction times (1-3 days) compared to ATRP, and only styrene and 4-vinylpyridine polymerizations proceed with good control of molecular weight and polydispersity.…”
Section: -15c Stable Free-radical Polymerization (Sfrp)mentioning
confidence: 99%