A model equation derived for the viscosity-average degree of polymerization (P.) for the incremental addition of modifiers, P, = K ( (exp{arzl] indicates a minimum should occur in a curve of P. versus conversion at which the increments are added, zl. Incremental addition of commercial tertdodecyl mercaptan in the laboratory to SBR recipes a t 5°C. showed effects contrary to those predicted by the model equation, but incremental addition experiments with tert-nonyl mercaptans resulted in a minimum in viscosity versua 21 curves, changed the molecular weight distribution, and required 34 wt.-% less mercaptan than did the tert dodecyl mercaptan control (all the tertdodecyl mercaptan added initially). Incremental additioh of tertnonylmercaptan in pilot plant 20-gal. autoclave reactors gave essentially the same results found in the laboratory bottle experiments. The stress4rain and mixing properties of the incrementally modified polymer and the tertdodecyl mercaptanmodified control were essentially the same within experimental error. Conditions required for successful application of the incremental modifier technique are given.