9300 Communications to the Editor
Macromolecules, Vol. 37, No. 25, 2004
For the synthesis of (N,N-butoxycarbonylmethyldithio-
carbamate), thiourea (17.2 g, 0.23 mol) and R,R,R′,R′-
tetramethyl-1,4-benzenedimethanol (20.0 g, 0.10 mol)
were mixed and added slowly with stirring to 48% HBr
(41.7 g, 0.25 mol). The slurry was heated to 50 °C, after
which the slurry solidified. The white solid was cooled,
filtered, washed with 0.1 mol/L aqueous HBr solution,
and dried under vacuum. The resulting white powder
was stirred for 2 h in aqueous NaOH (containing 0.62
mol of NaOH) at 40 °C. The resulting clear and red
solution was filtered, the red filtrate was cooled to 5 °C,
and under an Ar atmosphere a methyl isothiocyanate
(15.8 g, 0.22 mol) solution in methanol was added
dropwise. S-(1,4-Phenylenebis(propane-2,2-diyl)) bis(N-
methyldithiocarbamate) readily precipitated out as a
white solid. After filtration and washing with cold water,
the white solid was recrystallized twice from ethanol
and dried under vacuum. The overall yield was 60%.
Figure 1. Number-average molar mass (Mh n, b) and polydis-
persity index (PDI, ∆) vs conversion of the mimiemulsion
polymerization of n-butyl acrylate (BA), using the “butyl-
RAFT” agent. Drawn line is theoretical Mh n. Conditions: 3 h,
70 °C; organic phase: 8.0 g of BA, 2 wt % hexadecane with
respect to BA, 4.4 × 10-2 mol of “butyl-RAFT” per Lorganic phase
;
aqueous phase: 30 g of water, 2.3 × 10-3 mol of sodium dodecyl
sulfate (SDS) per Lwater, 3.0 × 10-3 mol of potassium peroxo-
disulfate per Lwater
.
1
Purity was confirmed with H and 13C NMR spectros-
copy and with LC-MS (MNa+ experimental: 395.01;
theoretical: 395.07).
measured values for Mh n are somewhat higher than the
calculated values, which might be explained by the fact
that the measured molecular weights are expressed in
polystyrene equivalents.
In another miniemulsion polymerization experiment,
10 wt % of the BA monomer was successfully substi-
tuted by methacrylic acid (MA), leaving the rest of the
variables exactly the same. For this polymerization, the
theoretical and experimental Mh n were 20 100 and 22 500
g/mol, respectively, and the polydispersity index after
92% conversion was 1.48. So, relatively polar blocks with
a controlled length can be synthesized using this new
concept.
n-Butyl chloroformate (3.1 g, 23 mmol) was dissolved
in THF (10 mL) and brought under an Ar atmosphere.
The mixture was cooled to -20 °C. S-(1,4-Phenylenebis-
(propane-2,2-diyl) bis(N-methyldithiocarbamate) (4.0 g,
11 mmol) and triethylamine (5.4 g, 54 mmol) were
dissolved in THF. This solution was added drop-by-drop
to the cold n-butyl chloroformate. The mixture was
stirred for 48 h, after which it was brought back to room
temperature. Triethylamine hydrochloride was filtered
off, and THF was removed under reduced pressure. The
resulting yellow oil was purified by column chromatog-
raphy using dichloromethane as the eluent and yielded
N,N-butoxycarbonylmethyldithiocarbamate as a yellow
The poly(butyl acrylate) latex described above was
applied as a seed latex for the polymerization of the
second monomer isooctyl acrylate (iOA). This seed latex
had a Mh n of 23 500 g/mol after 90% monomer conversion
(see Figure 1). The amount of iOA used was 3.0 g,
whereas 15 g of BA seed latex was used. The amount of
water was 12.0 g, and the (fresh) KPS concentration was
0.003 mol/L. For this seeded emulsion polymerization,
yielding a triblock copolymer, Mh n increases linearly with
iOA conversion.
Although the experimental part only describes the
detailed synthesis of a difunctional butyl-RAFT agent,
a multifunctional RAFT agent containing on average 12
RAFT groups (“poly(decyl-RAFT)” with R ) decyl and
naverage ) 6 in Scheme 1) was synthesized using a
difunctional chloroformate (for conditions, see Scheme
1). The yield was 70%. Figure 2 shows Mh n and PDI vs
BA conversion for this multifunctional RAFT agent.
For this homopolymerization of BA, for which the
conditions were comparable to those applied using the
difunctional butyl-RAFT agent, Mh n increases linearly
with conversion, indicating that also for this multifunc-
tional RAFT agent the radical polymerization occurs in
a controlled way. This polymer shows a good match of
the measured and calculated Mh n value after 85% BA
conversion (Mh n,exp ) 97 000 g/mol, Mh n,calc ) 99 500 g/mol,
PDI ) 3.1, average latex particle size ) 207 nm). On
the other hand, the molar mass distribution is relatively
broad, which is related to the high PDI of the “poly-
(decyl-RAFT)” itself, being 1.59. This high PDI is
inherent in the step-growth polymerization technique,
used to synthesize the multifunctional RAFT agent (see
Scheme 1).
1
liquid. Yield: 85%. Purity was confirmed with H and
13C NMR spectroscopy and with LC-MS (MNa+ experi-
mental: 595.76; theoretical: 595.84).
For the miniemulsion polymerizations, N,N-butoxy-
carbonylmethyldithiocarbamate (the “butyl-RAFT” agent)
was dissolved under stirring in a mixture of monomer
and hexadecane, comprising the organic phase. Sodium
dodecyl sulfate (SDS) was dissolved in water, and the
organic phase was added dropwise to the aqueous phase
under vigorous stirring. The preemulsion was sonicated
for 30 min. After emulsification, the miniemulsion was
transferred into an emulsion reactor under an argon
atmosphere, equipped with a reflux cooler and a ther-
mocouple. The miniemulsion was heated to 70 °C under
stirring, and potassium peroxodisulfate (KPS), dissolved
in water, was added, after which polymerization was
performed for 3 h. At regular time intervals, samples
were taken for gravimetric conversion measurement and
GPC analysis, using PS standards. The seed latexes,
obtained after the described polymerization () forma-
tion first block), were swollen overnight at room tem-
perature with a fresh amount of monomer, after which
the second polymerization step was performed under
argon, as described for the first step, using fresh KPS.
In one miniemulsion polymerization experiment, 8.0
g of n-butyl acrylate (BA) was polymerized, using 2 wt
% hexadecane with respect to the monomer and using
0.044 mol of difunctional butyl-RAFT agent/L. In the
aqueous phase (30 g), 0.0023 mol/L SDS and 0.0030
mol/L KPS were present. Figure 1 shows the linear
increase of Mh n with conversion, which is a good indica-
tion that the addition of the butyl-RAFT agent resulted
in a good control of the radical polymerization. The
The BA latex, obtained in the miniemulsion polym-
erization with the multifunctional RAFT agent de-