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. Author manuscript; available in PMC: 2013 Dec 10.
Published in final edited form as: Org Lett. 2012 May 8;14(10):2634–2637. doi: 10.1021/ol301007h

Table 2.

One-pot, sequential RCM/CM/chemoselective hydrogenation involving type II olefins

entry olefin yield %a
(avg %)
RCM-CM-chemoselective
hydrogenation
1 graphic file with name nihms-376255-t0020.jpg 41%
(75%)
graphic file with name nihms-376255-t0021.jpg
2 graphic file with name nihms-376255-t0022.jpg 35%
(71%)
graphic file with name nihms-376255-t0023.jpg
3 graphic file with name nihms-376255-t0024.jpg 69%
(89%)
graphic file with name nihms-376255-t0025.jpg
4 graphic file with name nihms-376255-t0026.jpg 48%
(78%)
graphic file with name nihms-376255-t0027.jpg
5 graphic file with name nihms-376255-t0028.jpg 72%
(90%)
graphic file with name nihms-376255-t0029.jpg
6 graphic file with name nihms-376255-t0030.jpg 30%b
(67%)
graphic file with name nihms-376255-t0031.jpg
7 graphic file with name nihms-376255-t0032.jpg 54%
(81%)
graphic file with name nihms-376255-t0033.jpg
8 graphic file with name nihms-376255-t0034.jpg 85%
(95%)
graphic file with name nihms-376255-t0035.jpg
9 graphic file with name nihms-376255-t0036.jpg 79%
(92%)
graphic file with name nihms-376255-t0037.jpg
a

All reactions were performed using freshly distilled (over CaH2) FDT solvents

b

Reaction was performed in CH2Cl2, 1,2-DCE purified by passing through basic Al2O3 and degassed by argon purging.