Progress in Organic Coatings 66 (2009) 99–106
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Progress in Organic Coatings
journal homepage: www.elsevier.com/locate/porgcoat
Styrenation of triglyceride oil by nitroxide mediated radical polymerization
Neslihan Alemdar
a
, A. Tuncer Erciyes
a,∗
, Yusuf Yagci
b,∗
a
Istanbul Technical University, Department of Chemical Engineering, 34469 Maslak, Istanbul, Turkey
b
Istanbul Technical University, Department of Chemistry, 34469 Maslak, Istanbul, Turkey
article info
Article history:
Received 13 January 2009
Received in revised form 9 April 2009
Accepted 15 June 2009
Keywords:
Styrenated oil
Controlled/living polymerization
NMRP
abstract
Styrenated oil was obtained by nitroxide mediated radical polymerization (NMRP) method in the pres-
ence of 2,2
′
,6,6
′
-tetramethylpiperidinyl-1-oxy (TEMPO). For this purpose, firstly, macroinitiator having
thermally unstable azo groups was obtained with reaction of partial glycerides (PGs) mixture and 4,4
′
-
azobis-4-cyanopentanoyl chloride (ACPC). Then, the macroinitiator was subjected to polymerization with
styrene in the presence of TEMPO in order to obtain a copolymer with controlled structure and low poly-
dispersity. The products thus obtained were characterized by GPC,
1
H NMR and FT-IR measurements.
A classical styrenated oil was also prepared for comparison. The film properties of the products were
determined according to the related standards and compared with each other. The product obtained at
the end of the 72h in the presence of TEMPO showed to some extent brittle film properties. To improve
the film properties, this product was further reacted with the oil-based vinyl macromonomer (MM).
The styrenated oil samples prepared by the controlled polymerization method, exhibited relatively low
polydispersity (<1.5) and showed good film properties.
© 2009 Elsevier B.V. All rights reserved.
1. Introduction
Over the past decade, nitroxide mediated radical polymeriza-
tion (NMRP) [1–4], together with the other equally important
controlled/living radical polymerization (CLRP) techniques such
as reversible addition–fragmentation chain transfer polymeriza-
tion (RAFT) [5–8] and atom transfer radical polymerization (ATRP)
[9–12] have generated a great deal of attention because of its ver-
satility in producing complex macromolecular architectures with
pre-estimated molecular weights and very narrow polydispersity
(M
w
/M
n
). Moreover, CLRP methods do not require strict purifica-
tion of monomers and solvents and tolerate a variety of functional
groups. For these reasons, they have more advantages than the
anionic polymerization technique [13].
∗
Corresponding authors.
E-mail addresses: erciyes@itu.edu.tr (A.T. Erciyes), yusuf@itu.edu.tr (Y. Yagci).
NMRP method is conducted in two steps. First, the reactions are
carried out at temperatures where initiation is rapid and all of the
chains are formed in about at the same time. In the second step, the
initiated polymer chains are reversibly capped by a stable free radi-
cal such as 2,2
′
,6,6
′
-tetramethylpiperidinyl-1-oxy (TEMPO), to give
a dormant living polymer. So, it provides control over the polymer-
ization system owing to this equilibrium. This equilibrium is given
by Eq. (1) [14].
(1)
NMRP has advantages over ATRP and RAFT as the resulting poly-
mer is not contaminated with metal ions and avoids the use of
malodorous sulfur compounds, respectively [15].
Triglyceride oils are widely used in the production of organic
coating materials. In order to obtain better film properties in coating
applications, oils are modified with various methods. Among these
methods copolymerization of oils with vinyl monomers occupies
an important place, styrene being the most widely used monomer
[16–23]. In the classical styrenation process, homopolystyrene for-
mation is likely to occur and the presence of homopolymer leads
to poor film properties. By taking this fact into account, the meth-
ods by which homopolymerization can be minimized and polymer
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doi:10.1016/j.porgcoat.2009.06.006