To use all functions of this page, please activate cookies in your browser.
With an accout for my.chemeurope.com you can always see everything at a glance – and you can configure your own website and individual newsletter.
- My watch list
- My saved searches
- My saved topics
- My newsletter
Autoacceleration (Gel Effect, Trommsdorff-Norrish Effect) is a dangerous reaction behavior that can occur in free radical polymerization systems. It is due to the localized increases in viscosity of the polymerizing system that slow termination reactions. The removal reaction obstacles therefore causes a rapid increase in the overall rate of reaction, leading to possible reaction runaway and altering the characteristics of the polymers produced.1
Additional recommended knowledge
Autoacceleration of the overall rate of a free radical polymerization system has been noted in many bulk polymerization systems. The polymerization of methyl methacrylate, for example, deviates strongly from classical mechanism behavior around 20 percent conversion; in this region the conversion and molecular weight of the polymer produced increases rapidly. This increase of polymerization is usually accompanied by a large rise in temperature if heat dissipation is not adequate. Without proper precautions, autoacceleration of polymerization systems could cause metallurgic failure of the reaction vessel or, worse, explosion.3
Norrish and Smith, Trommsdorff, and later, Schultz and Harborth, concluded that autoacceleration must be caused by a totally different polymerization mechanism. They rationalized through experiment that a decrease in the termination rate was the basis of the phenomenon. This decrease in termination rate, kt, is caused by the raised viscosity of the polymerization region when the concentration of previously formed polymer molecules increases. Before autoacceleration, chain termination by combination of two free radical chains is a very rapid reaction that occurs at very high frequency (about one in 10^4 collisions).1 However, when the growing polymer molecules with active free radical ends are surrounded in the highly viscous mixture consisting of a growing concentration of ‘dead’ polymer, the rate of termination becomes limited by diffusion. 2,3 The Brownian motion of the larger molecules in the polymer ‘soup’ are restricted, therefore limiting the frequency of their effective (termination) collisions.
With termination collisions restricted, the concentration of active polymerizing chains and simultaneously the consumption of monomer rises rapidly. Although viscosity affects the macromolecules, it does not prove high enough to prevent smaller molecules such as the monomer from moving relatively freely. Therefore, at the propagation reaction of the free radical polymerization process is relatively insensitive to changes in viscosity1 (this assumption does not hold true at high levels of monomer conversion).3 This also implies that at the onset of autoacceleration the overall rate of reaction increases relative to the rate of unautoaccelerated reaction given by the overall rate of reaction equation for free radical polymerization:
Rp = kp * [M] * ((f * kd * [I]) / kt)(1 / 2)
Qualitatively, as the termination decreases by a factor of 4, the overall rate of reaction will double. The decrease of termination reactions also allows radical chains to add monomer for longer time periods, raising the weight average molecular weight dramatically. However, the number average molecular weight only increases slightly, leading to broadening of the molecular weight distribution (high polydispersity index, very polydispersed product).3
Categories: Polymer chemistry | Reaction mechanisms
|This article is licensed under the GNU Free Documentation License. It uses material from the Wikipedia article "Autoacceleration". A list of authors is available in Wikipedia.|