Micro mixing effects in continuous radical polymerization View Full Text


Ontology type: schema:Chapter     


Chapter Info

DATE

2000

AUTHORS

Thomas Bayer , Detlev Pysall , Olaf Wachsen

ABSTRACT

In this study the development of a continuous radical solution polymerization process for acrylates in a lab scale tube reactor was performed. Fouling in the reactor was always observed if there were bad mixing conditions at the feed point of the reactor. In order to increase the homogenization of monomer and initiator a micro mixer was installed at the reactor inlet. The micro mixer ensured a very fast mixing at the micro scale of the preheated monomer and initiator solutions, and fouling was reduced tremendously. The reactor employed has a theoretical production capacity of 50 metric tons per year. A first prebasic design has shown that a production capacity of some thousand tons per year can be achieved by numbering up instead of conventional scale up. More... »

PAGES

165-170

Book

TITLE

Microreaction Technology: Industrial Prospects

ISBN

978-3-642-64104-6
978-3-642-59738-1

Author Affiliations

Identifiers

URI

http://scigraph.springernature.com/pub.10.1007/978-3-642-59738-1_15

DOI

http://dx.doi.org/10.1007/978-3-642-59738-1_15

DIMENSIONS

https://app.dimensions.ai/details/publication/pub.1050917910


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