Abstract Continuous reactors are important for commercial production of latex products and they can be useful tools for fundamental polymerization kinetics studies. Results are presented for four projects: (i) elimination of conversion oscillations in continuous stirred‐tank reactors (CSTR) by use of a tubular prereactor; (ii) use of a seed‐fed CSTR to measure free radical transport from monomer‐swollen latex particles; (iii) development of a continuous process as an alternative to a commercial batch process; and (iv) determination of copolymerization kinetic parameters with a steady‐state CSTR system.
Alexander PenlidisJohn F. MacGregorA. E. Hamielec
Jan MeuldijkC. J. G. van StrienF.A.H.C. van DoormalenD. Thoenes
V.I. LukhovitskiiV.I Listratov