|
|
|
|
LEADER |
01489 am a22001933u 4500 |
001 |
109210 |
042 |
|
|
|a dc
|
100 |
1 |
0 |
|a Mo, Yiming
|e author
|
100 |
1 |
0 |
|a Massachusetts Institute of Technology. Department of Chemical Engineering
|e contributor
|
100 |
1 |
0 |
|a Mo, Yiming
|e contributor
|
100 |
1 |
0 |
|a Jensen, Klavs F
|e contributor
|
700 |
1 |
0 |
|a Jensen, Klavs F
|e author
|
245 |
0 |
0 |
|a A miniature CSTR cascade for continuous flow of reactions containing solids
|
260 |
|
|
|b Royal Society of Chemistry, The,
|c 2017-05-19T15:51:24Z.
|
856 |
|
|
|z Get fulltext
|u http://hdl.handle.net/1721.1/109210
|
520 |
|
|
|a Continuous handling of solids creates challenges for realizing continuous production of pharmaceuticals and fine chemicals. We present a new miniature continuous stirred-tank reactor (CSTR) cascade to handle solid-forming reactions in flow. Single-phase residence time distribution (RTD) measurements of the CSTR cascade reveal nearly ideal CSTR mixing behavior of the individual units. Consistency of experimental and predicted conversions of a Diels-Alder reaction further confirms the CSTR performance. Two solid-forming reactions, (i) glyoxal reacting with cyclohexylamine to form N,N'-dicyclohexylethylenediimine, (ii) sulfonylation of 2-octanol with methanesulfonyl chloride, demonstrate the ability of the reactor cascade to transport solid particles continuously for hours without significant signs of clogging.
|
546 |
|
|
|a en_US
|
655 |
7 |
|
|a Article
|
773 |
|
|
|t Reaction Chemistry & Engineering
|