32
R
n
• + M → R
n+1
•
where R
n
• denotes
polymer chain with n mers, M – monomer, R
n+1
•– polymer chain
extended by one mer.
Termination can occur by combination:
R
x
• + R
y
• → R
x+y
or disproportionation:
R
x
• + R
y
• → R
x
+ R
y
[62]
.
Free radicals are highly reactive. A radical attacks a molecule of monomer,
initiating a macroradical, to which other monomer units are added successively. Each time
the active centre is transferred to the attached mer. This is the way in which propagation of
polymer chain occurs.
As
the reaction proceeds, the amount of monomer decreases, interpolymeric
reactions start to occur. Active parts of macroradicals meet each other and termination
takes place. It leads to dead polymer and may occur via combination or disproportionation.
The main disadvantage of this kind of polymerization
are problems with the
dissipation of the exothermicity in the sample volume. In effect, local hot spots are
formed [63]. During
free radical polymerization, an autoacceleration occurs, which is
known as Trommsdorff or gel effect [64]. This is a phenomenon of spectacular increase of
polymerization rate.
When the reaction speeds up, viscosity grows and huge amounts of
heat that are released accelerate this reaction further [65].
Trommsdorff effect occurs at high conversion,
when termination reactions
dominate and “dead” polymers, without active parts are produced. The vast majority of
polymer chains are long and slightly mobile. They are so immobilized that their fastest
termination
is with short, mobile, unentangled chains. Gel effect leads to uncontrolled local
rise of temperature what may result in the reactor explosion [66].
The other disadvantage of the bulk polymerization is that during the process the
polymerization shrinkage occurs. The most of the shrinkage appears in the early stages of
polymerization. It covers about 20 per cent of the initial volume. The shrinkage is a cause
of cracks and many other flaws like empty void in a block of polymer [67]. This is very
33
disfavourable in case of plastic scintillators because optical homogeneity of the material is
essential to provide the proper performance of the detectors.
However, conducting scintillators synthesis with the temperature schedule which is
presented in Fig. 9 enables to obtain samples without defects. Firstly the reaction mixture
is quickly heated to 100 °C and then to 140 °C within few hours. Next,
the principal
heating occurs and lasts about 70 hours. After this time, monomer is reacted into polymer
and the sample is cooled slowly to 90 °C. The scintillator is stored in this temperature for
three hours in order to anneal the sample. Then the scintillator is finally quenched.
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