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The “Did you know….?” series is a quarterly note from EPCEd that is intended to present simple questions about topics that are important to those working in the emulsion polymers area. Short and concise answers to those questions are presented to educate readers and to elicit comments and further discussion. Some readers will already know the answers and be familiar with the topic while others, especially newer to the field, will benefit from the answers and discussion. We welcome feedback from readers of this series through our contact website www.epced.com.
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“Did you know? April-June 2026"
Did you know .......... that chain transfer agents (CTA) arc used to limit the extent of crosslinking
in emulsion polymerizations (EP) of synthetic rubbers (think polybutadiene, PBd)? These rubbers
gain their elasticity via the crosslinking that naturally occurs in the /at/er portions of the latex
reaction. This issue of our •"Did you know .... "presentations is the 5th in a multi-part series that
collectively discusses the molecular weights typically produced in both batch and semi-batch
emulsion polymerization (EP) processes. the effectiveness of chain transfer agents (CTA) in both
process types~ and the possibility of polymer chain branching and cross-linking in the latex
particles. In the current issue we address the mechanism by which the CTA limits the crosslink
density of synthetic rubbers produced in latex form.
In general, linear polymer chain lengths produced in free radical polymerizations depend upon the
rate of propagation of the polymer radical and the rate at which chain growth is stopped (due to
termination or chain transfer). the so-called initiation, propagation, termination sequence. This is
certainly true in EP. Here we have latex particles constantly receiving oligomeric radicals
(typically containing ~3-6 monomer units) from the aqueous phase - some of these radicals grow
into high M\V polymer and some terminate other polymer radicals already in the particles. When
butadiene is the monomer (often with a small amount of styrene or acrylonitrile comonomer) and
the latex reaction is carried out as a batch process, the probability of crosslinking reactions
occurring increases as the monomer concentration in the latex particles decreases (as you may
know, this monomer reduction proceeds uniformly during the last -60% of the batch reaction).
Should the producer wish to limit the extent of crosslinking from its uncontrolled value~ the
addition of CTA can accomplish that task.
The mechanism of crosslinking involves a series of chemical reactions. The first, of course, is the
production of linear chains propagating within the latex panicle that already contains dead polymer
chains. The second involves proton transfer from the propagating chains to the backbone of the
existing dead polymer chains, thus creating a '"mid-chain radical'· on the otherwise dead polymer
chain. Eventually, this mid-chain radical adds a monomer unit and a branched, radical chain is
created that propagates with time. At last, two of these propagating branched chains terminate by
recombination, linking the two original dead (and maybe linear) chains. Although the detailed
mechanism can be more complicated than this, the above description will serve adequately to now
introduce the role of a CTA in altering the probability of one or more of the above reactions taking
place.
There are 2 types of polymer radical chains in the latex particle at any point in time - linear chains
and branched chains. The CTA can interact with both of these~ but the ones leading to crosslinking
control are the branched. radical chains. When that happens. the branch is terminated by proton
abstraction with the CTA (e.g. C12H21SH) and the possibility of that branch leading to crosslinking
is eliminated. In that W:t) the suppre~s1on of crosslinking from its unmodified level (that without
CTA) can be controlled by the type and level of the CTA in the latex recipe. This has been known
for more than 80 years the famous GRS Rubber Latex recipe developed in the 1940s for the
production of automotive tires is shown below.
Water 180 parts
1-3 butadiene 75 parts
Styrene 25 parts
"Soap" 5 parts
Mercaptan (t-dm) 0.5 parts
Potassium persulfate 0.3 parts
Ferrous sulfate 0.1 parts
We invite your questions and comments via our website, epced.com