ABSTRACT
In the last few years, high-throughput (HT) reactors have received significant attention due to the potential for fast material development. Split-plot experimental design plays a critical role in this type of application given randomization restrictions often imposed by equipment constraints. A case study in a parallel polymerization reactor is presented.
ACKNOWLEDGMENTS
The author thanks Professor Soren Bisgaard for his feedback and encouragement to publish the work reported in this article.
Notes
1Here, the designation well is used for individual reaction or synthesis chambers that are chemically isolated from other chambers and form the basic experimental unit of high-throughput experimentation.
2A module is a block of wells tied together by engineering constraints, such as a common pressure control unit or a common heater block.
3PPR is a registered trademark of Symyx Technologies, Santa Clara, California.
4 T = temperature, P = pressure, C = catalyst type, D = catalyst concentration.
5Ø2 is used to represent a fixed effect that is the sum squares of the model component associated with the particular factor divided by its degrees of freedom: is the fixed effect for catalyst type (C).