Subscribe to RSS
DOI: 10.1055/s-0030-1258487
Chemical Synthesis with Inductively Heated Copper Flow Reactors
Publication History
Publication Date:
09 July 2010 (online)
Abstract
Inductively heated copper wire inside a flow microreactor can serve as a source for a catalytic copper species that promotes 1,3-dipolar cycloadditions of alkynes with in situ formed azides to yield 1,2,3-triazoles. The same setup was used to carry out decarboxylations of 2-alkynoic acids and for the intramolecular C-O coupling of 2′-bromobiphenyl-2-carboxylic acid.
Key words
click chemistry - copper - heterogeneous catalysis - microreactors - inductive heating
- 1
Kirschning A.Solodenko W.Mennecke K. Chem. Eur. J. 2006, 12: 5972 -
2a
Larhed M.Hallberg A. Drug Discovery Today 2001, 6: 406 -
2b
Bogdal D.Loupy A. Org. Process Res. Dev. 2008, 12: 710 -
2c
Kappe CO. Chem. Soc. Rev. 2008, 37: 1127 -
3a
Welton T. Chem. Rev. 1999, 99: 2071 -
3b
Wasserscheidt P.Keim W. Angew. Chem. Int. Ed. 2000, 39: 3772 -
3c
Sheldon R. Chem. Commun. 2001, 2399 -
3d
Dupont J.de Souza RF.Suarez PAZ. Chem. Rev. 2002, 102: 3667 -
3e
Parvulescu VI.Hardacre C. Chem. Rev. 2007, 107: 2615 -
3f
Tzschucke CC.Markert C.Bannwarth W. Angew. Chem. Int. Ed. 2002, 41: 3964 -
3g
Ionic
Liquids
Wasserscheidt P.Welton T. Wiley-VCH; Weinheim: 2008. - Selected reviews on flowthrough systems in organic synthesis:
-
4a
Jas G.Kirschning A. Chem. Eur. J. 2003, 9: 5708 -
4b
Kirschning A.Jas G. In Immobilized Catalysts, Topics in Current Chemistry Vol. 242:Kirschning A. Springer; Berlin/Heidelberg: 2004. p.209-239 -
4c
Baxendale IR.Ley SV. In New Avenues to Efficient Chemical Synthesis: Emerging TechnologiesSeeberger PH.Blume T. Springer; Berlin/Heidelberg: 2007. p.151-185 -
4d
Baxendale IR.Hayward JJ.Lanners S.Ley SV.Smith CD. In Microreactors in Organic Synthesis and CatalysisWirth T. Wiley-VCH; Weinheim: 2008. Chap. 4.2. p.84-122 -
4e
Ahmed-Omed B.Brandt JC.Wirth T. Org. Biomol. Chem. 2007, 5: 733 -
4f
Mak XY.Laurino P.Seeberger PH. Beilstein J. Org. Chem. 2009, 19 -
4g
Wiles C.Watts P. Eur. J. Org. Chem. 2008, 10: 1655 -
4h
Ley SV.Baxendale IR. CHIMIA 2008, 62: 162 -
4i
Ahmed-Omer B.Brandt JC.Wirth T. Org. Biomol. Chem. 2007, 5: 733 -
4j
Ceylan S.Kirschning A. In Recoverable and Recyclable CatalystsBenaglia M. John Wiley and Sons; Chichester: 2009. Chap. 13. p.379-411 -
4k
Yoshida J.Nagaki A.Yamada T. Chem. Eur. J. 2008, 14: 7450 -
4l
Fukuyama T.Rahman MT.Sato M.Ryu I. Synlett 2008, 151 -
4m
Mason BP.Price KE.Steinbacher JL.Bogdan AR.McQuade DT. Chem. Rev. 2007, 107: 2300 - Reviews on immobilised catalysts:
-
5a In Immobilized Catalysts,
Topics in Current Chmistry
Vol. 242:
Kirschning A. Springer; Berlin/Heidelberg: 2004. -
5b
Solodenko W.Frenzel T.Kirschning A. In Polymeric Materials in Organic Synthesis and CatalysisBuchmeiser MR. Wiley-VCH; Weinheim: 2003. -
5c
McNamara CA.Dixon MJ.Bradley M. Chem. Rev. 2002, 102: 3275 -
5d
McMorn P.Hutchings GJ. Chem. Soc. Rev. 2004, 33: 108 -
6a
Kunz U.Kirschning A.Altwicker C.Solodenko W. J. Chromatogr., A 2003, 1006: 241 -
6b
Kunz U.Schönfeld H.Solodenko W.Jas G.Kirschning A. Ind. Eng. Chem. Res. 2005, 44: 8458 -
6c
Kunz U.Kirschning A.Wen H.-L.Solodenko W.Cecillia R.Kappe CO.Turek T. Catal. Today 2005, 105: 318 -
7a
Kirschning A.Altwicker C.Dräger G.Harders J.Hoffmann N.Hoffmann U.Schönfeld H.Solodenko W.Kunz U. Angew. Chem. Int. Ed. 2001, 40: 3995 -
7b
Solodenko W.Kunz U.Kirschning A. Bioorg. Med. Chem. Lett. 2002, 12: 1833 -
8a
Kunz U.Leue S.Stuhlmann F.Sourkouni-Argirusi G.Wen H.Jas G.Kirschning A. Eur. J. Org. Chem. 2004, 3601 -
8b
Kirschning A.Mennecke K.Kunz U.Michrowska A.Grela K. J. Am. Chem. Soc. 2006, 128: 13261 -
8c
Solodenko W.Jas G.Kunz U.Kirschning A. Synthesis 2007, 583 -
8d
Dräger G.Kiss C.Kunz U.Kirschning A. Org. Biomol. Chem. 2007, 5: 3657 -
8e
Kirschning A.Mennecke K.Solodenko W. Synthesis 2008, 1589 -
8f
Mennecke K.Kirschning A. Synthesis 2008, 3267 - 9
Mennecke K.Cecilia R.Glasnov TN.Gruhl S.Vogt C.Feldhoff A.Larrubia Vargas MA.Kappe CO.Kunz U.Kirschning A. Adv. Synth. Catal. 2008, 350: 717 -
10a
Ceylan S.Friese C.Lammel Ch.Mazac K.Kirschning A. Angew. Chem. Int. Ed. 2008, 47: 8950 ; Angew. Chem. 2008, 120, 9083 -
10b
Wegner J.Ceylan S.Friese C.Kirschning A. Eur. J. Org. Chem. 2010, in press -
11a
Lu A.-H.Salabas EL.Schüth F. Angew. Chem. Int. Ed. 2007, 46: 1222 ; Angew. Chem. 2007, 119, 1242 -
11b
Jun Y.-W.Choi J.-S.Cheon J. Chem. Commun. 2007, 1203 -
11c
Zhang XK.Li YF.XiaoJ Q.Wetzel ED. J. Appl. Phys. 2003, 93: 7124 - 12
Hiergeist R.Andrä W.Buske N.Hergt R.Hilger I.Richter U.Kaiser WJ. J. Magn. Magn. Mater. 1999, 201: 420 - 13
Ley SV.Thomas AW. Angew. Chem. Int. Ed. 2003, 24: 5400 - 14
Tornøe CW.Christensen C.Meldal M. J. Org. Chem. 2002, 67: 3057 -
15a
Kolb HC.Finn MG.Sharpless KB. Angew. Chem. Int. Ed. 2001, 40: 2004 -
15b
Rostovtsev VV.Green LG.Fokin VV.Sharpless KB. Angew. Chem. Int. Ed. 2002, 41: 2596 - 16
Smith CD.Baxendale IR.Lanners S.Hayward JJ.Smith SC.Ley SV. Org. Biomol. Chem. 2007, 5: 1559 - 17
Bogdan AR.Sach NW. Adv. Synth. Catal. 2009, 351: 849 - 21
Kolarovic A.Faberova Z. J. Org. Chem. 2009, 74: 7199 - 22
Trost BM.Weiss AH. Org. Lett. 2006, 8: 4461 -
23a
Ley SV.Thomas AW. Angew. Chem. Int. Ed. 2003, 42: 5400 -
23b
Wolter M.Nordmann G.Buchwald SL. Org. Lett. 2002, 4: 973 -
23c
Liebeskind SL.Srogl J. Org. Lett. 2002, 4: 979 - 24
Thasana N.Worayuthakarn R.Kradanrat P.John E.Young L.Ruchirawat S. J. Org. Chem. 2007, 72: 9379
References and Notes
Quadrapure TU is commercially available from Sigma-Aldrich.
19Hazard warning: Aliphatic azides are regarded to be potentially explosive. Not for all azides that can occur as byproducts in the ‘click’ chemistry reactions data are available in the literature. We never encountered any hazards during these studies. However, this observation does not exclude the possibility of explosions.
20
Typical Procedure
for Triazole Syntheses
A glass reactor (12 cm length
and 8.5 mm internal diameter) was filled with copper wire (ca. 24
g) and incased with the inductor. The reactor (void volume: 2 mL)
was connected to the pump and at the outlet side to a scavenger
cartridge which was filled with QuadrapureTM TU. The
collection vial was placed behind the scavenger cartridge. The system
was flushed with a DMF-H2O mixture (5:1), and
the temperature was adjusted to 100 ˚C. After
the flow (flow rate 0.2 mL/min) and temperature values
reached a steady state a solution of bromide 4 (0.25
M), phenylacetylene (1, 0.125), and sodium
azide (0.25 M, higher concentrations led to blockage of the system
due to precipitation) in DMF-H2O was pumped
through the system (residence time approx. 10 min). After collection
of the crude product, the mixture was diluted with H2O,
extracted with EtOAc, and dried (MgSO4). After evaporation
of the solvent the crude product was purified by flash chromatography
on silica gel to yield compound 5 in quantitative
yield as a slightly yellow solid.
Typical Procedure
for the Catalytic Decarboxylation
A glass reactor
(12 cm length and 8.5 mm internal diameter) was filled with copper
wire (ca. 24 g) and incased with the inductor. The reactor (void
volume: 2 mL) was connected to the pump and at the outlet side to
a scavenger cartridge which was filled with QuadrapureTM TU.
The collection vial was placed behind the scavenger cartridge. The
system was flushed with MeCN, and the temperature was adjusted to 60 ˚C.
After the flow (flow rate 0.1 mL/min) and temperature values
reached a steady state a solution of 2-alkynoic acid 13 (0.1
M) in MeCN was pumped through the system (residence time approx.
20 min). After collection of the crude product, the solvent was
evaporated in vacuo, and the crude material was purified by flash
chromatography on silica gel to yield compound 14 in
93% yield as a yellow oil.
Synthesis of Benozopyranone
18
A PEEK reactor (12 cm length and 8.5 mm internal diameter)
was filled with copper wire (ca. 24 g) and incased with the inductor.
The reactor (void volume: 2 mL) was connected to the pump and on
the outlet side to a back pressure device (6.9 bar) which led to
a scavenger cartridge which was filled with QuadrapureTM TU.
Behind the scavenger cartridge the collection vial was placed. The system
was flushed with DMF, and the temperature was adjusted to 200 ˚C.
After the flow (flow rate 0.1 mL/min) and temperature values
reached a steady state a solution of bromo acid 17 (0.04
M) in DMF was pumped through the system (residence time approx.
20 min). After collection of the crude product, the mixture was
diluted with H2O, extracted with EtOAc, and dried (MgSO4).
After evaporation of the solvent in vacuo the crude product was purified
by flushing through a short pad of silica to yield compound 18 in 95% yield as a pale brownish
solid.