10.1002/adsc.201801240
Advanced Synthesis & Catalysis
under reduced pressure, affording a deep purple powder.
Yield: 1.5519 g, 77.8 %. Elemental analysis calcd. for
C50H86Br2FeNO2S2: C, 59.28; H, 8.56; N, 1.38; S, 6.33;
found: C, 59.34 H, 8.60; N, 1.50; S, 6.38. µeff = 5.76 µB at
30 °C.
Jerome, T. Tassaing, C. Detrembleur, Catal. Sci.
Technol. 2017, 7, 2651-2684; e) H. Zhou, X. Lu, Sci.
China: Chem. 2017, 60, 904-911; f) R. R. Shaikh, S.
Pornpraprom, V. D’Elia, ACS Catal. 2018, 8, 419-450.
g) X.-B. Lu, B. Liang, Y.-J. Zhang, Y.-Z. Tian, Y.-M.
Wang, C.-X. Bai, H. Wang, R. Zhang, J. Am. Chem.
Soc. 2004, 126, 3732-3733; h) T. Ema, Y. Miyazaki, S.
Koyama, Y. Yano, T. Sakai, Chem. Commun. 2012, 48,
4489-4491; i) C. J. Whiteoak, N. Kielland, V. Laserna,
E. C. Escudero-Adꢂn, E. Martin, A. W. Kleij, J. Am.
Chem. Soc. 2013, 135, 1228-1231; j) C. Maeda, J.
Shimonishi, R. Miyazaki, J.-Y. Hasegawa, T. Ema,
Chem. - Eur. J. 2016, 22, 6556-6563; k) F. Della
Monica, S. V. C. Vummaleti, A. Buonerba, A. De Nisi,
M. Monari, S. Milione, A. Grassi, L. Cavallo, C.
Capacchione, Adv. Synth. Catal. 2016, 358, 3231-3243.
Typical procedure for CO2/5a coupling (referred to
entry 16, Table 1). A 60 mL stainless steel pressure
reactor equipped with a magnetic stirring bar was charged,
under CO2 atmosphere, with 42.0 mg of catalyst 4 (4.15 ∙
10−5 mol) and 40.1 mg of TBAB (1.25 ∙ 10−4 mol)
dissolved in 5.0 mL of 5a (4.15 ∙ 10−2 mol). The reaction
mixture was pressurized with CO2 at 1 bar and stirred at
35 °C for 24 h. The reactor was cooled with ice, the CO2
released, 0.58 mL of mesitylene (4.15 ∙ 10−3 mol) was
added as an internal standard and the mixture was analyzed
1
by H NMR spectroscopy using CDCl3 as solvent (Figure
S23). Conversion = 92.0 %.
Typical procedure for CO2/epoxide coupling promoted
by 4 (referred to Scheme 5). A 60 mL stainless steel
pressure reactor equipped with a magnetic stirring bar was
charged, under CO2 atmosphere, with 84.0 mg of catalyst 4
(8.3 ∙ 10−5 mol) dissolved in 5.0 mL of 5a (4.15 ∙ 10−2 mol).
The reaction mixture was pressurized with CO2 at 1 bar and
stirred at 35 °C for 6 h. The reactor was cooled with ice,
the CO2 released, 0.58 mL of mesitylene (4.15 ∙ 10−3 mol)
was added as an internal standard and the mixture was
analyzed by 1H NMR spectroscopy using CDCl3 as solvent
(Figure S24). Conversion = 48.0 %.
[3]a) B. Schaffner, F. Schaffner, S. P. Verevkin, A. Borner,
Chem. Rev. 2010, 110, 4554-4581; b) M. Sathish, K. J.
Sreeram, J. Raghava Rao, B. Unni Nair, ACS
Sustainable Chem. Eng. 2016, 4, 1032-1040, c) S.
Lawrenson, M. North, F. Peigneguy, A. Routledge,
Green Chem. 2017, 19, 952-962; d) S. B. Lawrenson,R.
Arav, M. North, Green Chem. 2017, 19, 1685-1691.
Only for propylene carbonate 6b, the isolated yield was
determined because of the volatile nature of the epoxide
5b: the volatiles were removed under vacuum, the sample
treated with pentane to precipitate the catalyst, filtered over
silica and the solvent removed by rotary evaporation; yield
= 2.75 g (65%).
[4] a) X. L. Wei, W. Xu, M. Vijayakumar, L. Cosimbescu,
T. B. Liu, V. Sprenkle, W. Wang, Adv. Mater. 2014, 26,
7649-7653.
[5] a) C. Beattie, M. North, P. Villuendas, C. Young, J.
Org. Chem. 2013, 78, 419-426; b) V. Laserna, G.
Fiorani, C. J. Whiteoak, E. Martin, E. Escudero-Adan,
A. W. Kleij, Angew. Chem. Int. Ed. 2014, 53, 10416-
10419; c) S. H. Kim, K. H. Kim, S. H. Hong, Angew.
Chem. Int. Ed. 2014, 53, 771-774; d) H. L. Liu, Z. W.
Huang, Z. B. Han, K. L. Ding, H. C. Liu, C. G. Xia, J.
Chen, Green Chem. 2015, 17, 4281-4290; e) R. S. Kalb,
E. N. Stepurko, V. N. Emel’yanenko, S. P. Verevkin,
Phys. Chem. Chem. Phys. 2016, 18, 31904-31913.
Acknowledgements
Ministero dell’Istruzione dell’Universitꢀ e della Ricerca (MIUR,
Roma, Italy) and Universitꢀ degli Studi di Salerno (FARB 2016-
ORSA165551) are acknowledged for funding. The authors
acknowledge Dr. Patrizia Oliva, Dr. Patrizia Iannece, Dr.
Mariagrazia Napoli, and Dr. Ivano Immediata from University of
Salerno for technical assistance.
[6] a) V. Caló, A. Nacci, A. Monopoli, A. Fanizzi, Org.
Lett. 2002, 4, 2561-2563; b) F. Della Monica, A.
Buonerba, A. Grassi, C. Capacchione, S. Milione,
ChemSusChem 2016, 9, 3457-3464.
References
[1] a) Carbon Dioxide Recovery and Utilization, 1st ed.,
Ed.: M. Aresta, Springer Science+Business Media,
Dordrecht, 2003; b) Carbon Dioxide Utilization:
Closing the Carbon Cycle, 1st ed., Eds.: P. Styring, E. A.
Quadrelli, K. Armstrong, Elsevier, Amsterdam, 2015;
c) E. S. Sanz-Pꢀrez, C. R. Murdock, S. A. Didas, C. W.
Jones, Chem. Rev. 2016, 116, 11840-11876; d) A. J.
Hunt, E. H. K. Sin, R. Marriott, J. H. Clark,
ChemSusChem 2010, 3, 306-322; e) J. A. Martens, A.
Bogaerts, N. De Kimpe, P. A. Jacobs, G. B. Marin, K.
Rabaey, M. Saeys, S. Verhelst, ChemSusChem 2017, 10,
1039-1055; f) M. Aresta, A. Dibenedetto, A. Angelini,
Chem. Rev. 2014, 114, 1709-1742; g) J. Artz, T. E.
Mꢁller, K. Thenert, J. Kleinekorte, R. Meys, A.
Sternberg, A. Bardow, W. Leitner, Chem. Rev. 2018,
118, 434-504.
[7] a) M. North, R. Pasquale, Angew. Chem. Int. Ed. 2009,
48, 2946-2948; b) A. Buchard, M. R. Kember, K. G.
Sandeman, C. K. Williams, Chem. Commun. 2011, 47,
212-214; c) J. E. Dengler, M. W. Lehenmeier, S. Klaus,
C. E. Anderson, E. Herdtweck, B. Rieger, Eur. J. Inorg.
Chem. 2011, 3, 336-343; d) M. Adolph, T. A. Zevaco,
O. Walter, E. Dinjus, M. Döring, Polyhedron 2012, 48,
92-98; e) M. Adolph, T. A. Zevaco, C. Altesleben, O.
Walter, E. Dinjus, Dalton Trans. 2014, 43, 3285-3296;
f) F. M. Al-Qaisi, M. Nieger, M. L. Kemell, T. J. Repo,
ChemistrySelect 2016, 3, 545-548; g) F. Chen, N. Liu,
B. Dai, ACS Sustainable Chem. Eng. 2017, 5, 9065-
9075.
[8] F. Della Monica, B. Maity, T. Pehl, A. Buonerba, A. De
Nisi, M. Monari, A. Grassi, B. Rieger, L. Cavallo, C.
Capacchione, ACS Catal. 2018, 8, 6882-6893.
[2] a) X.-B. Lu, D. J. Darensbourg, Chem. Soc. Rev. 2012,
41, 1462-1484; b) J. W. Comerford, I. D. V. Ingram, M.
North, X. Wu, Green Chem. 2015, 17, 1966-1987; c) C.
Martín, G. Fiorani, A. W. Kleij, ACS Catal. 2015, 5,
1353-1370; d) M. Alves, B. Grignard, R. Mereau, C.
[9] F. Castro-Gómez, G. Salassa, A. W. Kleij, C. Bo, Chem.
Eur. J. 2013, 19, 6289-6298.
5
This article is protected by copyright. All rights reserved.