2015
DOI: 10.1021/acscatal.5b00002
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Asymmetric Organocatalysis in Continuous Flow: Opportunities for Impacting Industrial Catalysis

Abstract: The review highlights the different advantages associated with organocatalytic transformations performed in continuous-flow systems and presents the reactions which have been successfully achieved to date. Particular focus is placed on the comparison between batch and flow applications in order to show the advantages and disadvantages and to demonstrate the great potential for applying organocatalysis as well as combined organo and photoredox catalyzed reactions in continuous flow.

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Cited by 189 publications
(81 citation statements)
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“…[17][18][19][20][21][22][23][24][25][26][27][28][29] However, due to the extremelyf ast growthi no rganocatalyzed domino reactions,m anyn ew developments keep showing up on ad aily basis,w hich makes these reviews somewhat outdated very quickly.I na ddition, many of recentlyp ublished review articles on this topic are quite narrow in terms of theirs cope,f ocusing on either the synthesis of specific scaffolds or the processesm ediated by as pecific type of organocatalyst. [20][21][22][23][24][25][26][27][28][29] Due to the importance of this research and the fast developments in this area, we believe an ew review is needed and, in the present review,w ea re going to summarize the most recent developments in organocatalyzeda symmetric domino reactions,c overing the literature published from the beginning of 2012 up to May,2 017. Althoughs ome of the name reactions,such as the Mannich reactionand Biginelli reaction, are domino in nature,t hey are generally not covered in this review unless they are part of the entire domino reactions,b ecause there are many upto-date reviews out there dedicated to these name reactions.…”
Section: Introductionmentioning
confidence: 99%
“…[17][18][19][20][21][22][23][24][25][26][27][28][29] However, due to the extremelyf ast growthi no rganocatalyzed domino reactions,m anyn ew developments keep showing up on ad aily basis,w hich makes these reviews somewhat outdated very quickly.I na ddition, many of recentlyp ublished review articles on this topic are quite narrow in terms of theirs cope,f ocusing on either the synthesis of specific scaffolds or the processesm ediated by as pecific type of organocatalyst. [20][21][22][23][24][25][26][27][28][29] Due to the importance of this research and the fast developments in this area, we believe an ew review is needed and, in the present review,w ea re going to summarize the most recent developments in organocatalyzeda symmetric domino reactions,c overing the literature published from the beginning of 2012 up to May,2 017. Althoughs ome of the name reactions,such as the Mannich reactionand Biginelli reaction, are domino in nature,t hey are generally not covered in this review unless they are part of the entire domino reactions,b ecause there are many upto-date reviews out there dedicated to these name reactions.…”
Section: Introductionmentioning
confidence: 99%
“…Accordingly, during the last fifteen years, the development of heterogeneous recyclable organocatalysts became a significant task. 16,32,[148][149][150][151][152] Moreover, several efficient organocatalysts were able to catalyse various reactions or could tolerate the presence of other catalytic species. Thus, their application in one-pot reactions also evolved rapidly.…”
Section: One-pot Reactions Using Heterogenized Chiral Organocatalystsmentioning
confidence: 99%
“…Furthermore, the successful recycling of these heterogeneous catalysts has promoted their application in continuous-flow systems. 190,191 Sequential asymmetric reactions using immobilized reagents, chiral organocatalysts and scavengers placed in successive fixed-bed reactors provided the opportunity for the convenient preparation of optically pure fine chemicals. Similar to the one-pot reactions, during these processes, several purification steps may be eliminated; moreover, reactions occurring through sensitive, unstable, hazardous intermediates are easily carried out.…”
Section: 186mentioning
confidence: 99%
“…[1][2][3][4] However, trickle-bed reactors and slurry bubble columns are still the workhorses in the chemical industry for multiphase operations involving heterogeneously catalyzed reactions with gas-liquid reactants. While stirring in the slurry reactor prevents catalyst particles from settling and allows active mixing at high Reynolds numbers (minimizing temperature and concentration gradients), subsequent separation of the catalyst particles and partial replacement due to damage from attrition is required.…”
Section: Introductionmentioning
confidence: 99%