The feasibility of using continuous-flow tubular reactors (CFTR) as an efficient research tool for polymerization reactions is investigated. This is a continuation of the extensive effort that had been made at Dow in recent years to set up and employ an electro-thermal microreactor (an ohmically-heated CFTR), which resulted in several internal and external publications and a US Patent. The main focus of this work is to investigate the effect of operating conditions and flow composition, mainly the number of existing phases, on the molecular weight of the polymer. A series of polymerization experiments were performed in single-phase (liquid) and two-phase (vapor-liquid) flow regimes. In single-phase polymerization, the ethylene concentration falls continuously along the length of the reactor. This will have a significant effect on the kinetics of polymerization, particularly the molecular weight of the produced polymer. A key advantage of operating in the two-phase region is that an almost constant ethylene concentration is maintained along the length of the reactor. In effect, the vapor phase serves as a reservoir that replenishes the ethylene consumed in the liquid phase by polymerization. The molecular weight data show that this assumption is valid provided that the rate of mass transfer is significantly higher than the rate of the polymerization reaction.
IntroductionThe feasibility of using continuous-flow tubular reactors (CFTR) as an efficient research tool for polymerization reactions is investigated. The simple design and versatility of these reactors make them an attractive tool for conducting research on chemical reactions. This work is a continuation of the effort that had been made at Dow to make use of an electro-thermal microreactor (an ohmically-heated CFTR). The details of the operations and applications of this reactor have been extensively reported in several internal and external publications [1][2][3]. In summary, a tubing electro-thermal micro reactor (ETMR), which was ohmically heated, was developed and used for monitoring polymerization reactions at the milligram scale. This was a new approach based on the idea of using simple 1/16 in. steel tubing as an electrical heater, a conduit for the reactant solution mixture of interest, and the tubing wall itself as a multipoint temperature sensor array. The idea was to insulate the reactor (semi-adiabatic) and monitor the temperature profiles of the reactor's different zones, assuming that more active catalysts would result in higher observed temperature rises. Several polymerization experiments using different catalysts and reaction conditions were carried out to evaluate the performance of this reactor. Although the polymerization experiments seemed to run very well, the properties of the polymer samples produced, particularly the molecular weight, were not satisfactory. In summary, the observed low molecular weights in almost all the samples were attributed to two factors: 1) non-isothermal reaction conditions, and 2) the continuous decrease i...