SynopsisInitial rates of polymerization were meaaured a t 70.0 and 89.7"C. for styrene, p divinylbenzene, and mixtures of the two monomers initiated with 1% benzoyl peroxide. The r a h relative to styrene increased linearly with mole fraction of pdivinylbenzene; the latter monomer polymerized faster than styrene by rr factor of 2.50 at 70.0"C. and 3.54 a t 89.7"C. Times to gelation were also measured for those aamplea containing p divinylbenzene, and from thew times the correeponding fractional converaion at the gel point waa calculated. The conversion a t the gel point passed through a minimum with increasing content of pdivinylbenzene. The gelation behavior is explained by concurrent interchain croaalinking to give a network and intrachaii crosslinking to give microgels which accumulate to give macrogel, the latter process being dominant at all but low concentrations of p-divinylbenzene. The higher the content of crosslinker, the leaa swollen the microgels, and the greater the conversion required to give gelation by this process. The linear increase in rate with increasing pdivinylbenzene rontent was aho explained by intrachin crosslinking: growing polymer radicals which undergo this procem have a reduced rate of termination. The factor by which the termination rate constant is reduced with increasing divinylbenzene content ia the same factor aa that by which the conversion required to give gelation by accumula.tion of microgels is increased.
INTRODUCTIONThe copolymerization of divinylbenzene with styrene was first carried out by Staudinger' in order to demonstrate that crosslinking caused by the divinyl monomer would make the polystyrene insoluble in all solvents. In recent years, the insoluble gels obtained from copolymerization of these two monomers have become important as backbones for synthetic ion exchange resins. The properties of the finished copolymers have been studbut the copolymerization process itself has been virtually ignored. There is a practical reason for this: commercial divinylbenzene is a complex mixture containing both meta and para isoniers of divinylbenzcrie as well as other related hydrocarbons, and its composition is not a variable easily controlled in polymerization studies. This work was undertaken to remedy the lack of information on the rates and gel points of polymerizing styrenedivinylbenzene mixtures. The problems associated with commercial divinylbenzerie were avoided by using pure pdivinylbenzene, which can be separated from the commercial mixture by a brornination-debromination sequence.
The Problem of GelationWhc.11 a iiionoviiiyl iii~iioiiier is copolytiierized.with a diviiiyl tnotioiiicr, the rcactioii niass will usually gcl at a coiivorsion characteristic of thc: monom m and the reaction conditions. The transition from fluid to gel is that point a t which a gas bubble or glass ball moving gently through the polymerizing mixture suddenly becomes immobilized. 111 other words, it is that point at which the mixture appears to develop a very small but finite yield stress. Th...