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01345 am a22002413u 4500 |
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101199 |
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|a Abolhasani, Milad
|e author
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|a Massachusetts Institute of Technology. Department of Chemical Engineering
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|a Massachusetts Institute of Technology. Department of Chemistry
|e contributor
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|a Abolhasani, Milad
|e contributor
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|a Bruno, Nicholas C.
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|a Jensen, Klavs F.
|e contributor
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|a Bruno, Nicholas C.
|e author
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|a Jensen, Klavs F.
|e author
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|a Oscillatory three-phase flow reactor for studies of bi-phasic catalytic reactions
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|b Royal Society of Chemistry,
|c 2016-02-17T16:21:32Z.
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|z Get fulltext
|u http://hdl.handle.net/1721.1/101199
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|a A multi-phase flow strategy, based on oscillatory motion of a bi-phasic slug within a fluorinated ethylene propylene (FEP) tubular reactor, under inert atmosphere, is designed and developed to address mixing and mass transfer limitations associated with continuous slug flow chemistry platforms for studies of bi-phasic catalytic reactions. The technique is exemplified with C-C and C-N Pd catalyzed coupling reactions.
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|a Novartis-MIT Center for Continuous Manufacturing
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|a en_US
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|a Article
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|t Chemical Communications
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