Clogging is one of the major hurdles during continuous polymerization in microreactors, which makes their implementation difficult. In this work, the main factors affecting clogging in tubular microreactors used for the production of polymer dispersions by emulsion polymerization were investigated. Thus, the role of flow rate, residence time and solids content was analyzed. Further, strategies to reach higher conversion together with higher solids content without clogging were implemented. Pros and cons of feeding an extra amount of surfactant at a given point of the reactor were discussed. The addition of a bigger diameter tube after the microreactor was considered as a robust approach, since it allowed obtaining higher conversions without any obstruction in the reactor. However, miniemulsion polymerization was found as the most promising alternative because high conversion together with higher solids content were achieved at relatively low residence times, without diminishing the reactor operability. Monomers with fast rate of polymerization, such as butyl acrylate, were demonstrated to be the most appropriate for this type of reactors. (C) 2012 Elsevier B.V. All rights reserved.