Concurrent tandem catalysis

From Wikipedia, the free encyclopedia
Jump to: navigation, search
Scheme 1

Concurrent tandem catalysis (CTC) is a technique in chemistry which uses multiple catalysts on a single molecule in a one-pot reaction to produce a product otherwise not accessible by a single catalyst.[1] Scheme 1 illustrates this process. Molecule A enters this catalytic system to produce the comonomer, B, which along with A enters the next catalytic process to produce the final product, P. This one-pot approach can decrease product loss from isolation or purification of intermediates. Reactions with relatively unstable products can be generated as intermediates because they are only transient species and are immediately used in a consecutive reaction.


The major advantage of using CTC is it requires a single molecule; however, the required reaction conditions and catalyst compatibility are major hurdles to overcome. The system must be thoroughly studied to find the optimal conditions for both the catalysis and reactant to produce the desired product. Occasionally, a trade-off must be made between several competing effects.

The desire of getting better yields and selectivity is of interest to many in academia and the industry. In this one-pot system, intermediate purification isn’t necessary, so the risk of unwanted products and side reactions are more probable. The catalysis is the key to the catalytic system. Matching compatible catalysts would eliminate the likelihood of a catalyst starving or saturating the system, which may cause the catalyst to decompose or generate unwanted side reactions.[1] If side products were to be generated, it may be capable of interfering with the catalytic system. Thus in-depth knowledge is required of the mechanistic characteristics of both catalytic processes and the activity of the catalysts. Kinetic measurements are a crucial instrument in the development of CTC processes.




One of the simplest and most thoroughly studied polymers arises from the polymerization of ethylene. Linear low-density polyethylene, LLDPE, is of industrial importance and is currently produced on the macro- scale; millions of tons per year.[1] Branching of polyethylene involves the oligomerization of ethylene into alpha-olefins, carried out by one catalyst, followed by ethylene polymerization using the α-olefins as co-monomer, carried out by a second catalyst. This system was studied by Beach and Kissin which was found to have suffered in some inadequacies. It was found that the catalytic activity decreased as the concentration of catalyst increased due to poisoning of some of the catalyst centers.[2]

Work done by Bazan et al. found that addition of an electron deficient boron compound activated the phosphorus-oxygen chelated nickel catalyst to oligomerize ethylene into α-butylene. Then a titanium catalyst polymerizes ethylene and the α-olefin to form LLDPE. The degree of branching was found to increase linearly with the increase in concentration of the nickel catalyst.[3][4]



Metathesis has been a powerful tool in the coupling of olefins for several decades. The ability to rearrange carbon-carbon double bonds has provided great utility in all aspects of organic chemistry. Cossy et al. report a simple synthesis to form substituted five and six membered lactones from the cross metathesis of an allylic or homoallylic alcohol and acrylic acid using a ruthenium based metathesis catalyst. Lactones are good synthetic starting points for many natural products and are prevalent structures in biology therefore they are widely utilized in pharmaceuticals.[5]



One of the most studied and commercially important transition metal catalyzed reactions is alkene hydroformylation. This type of catalysis allows for the functionalization of simple alkenes into aldehydes and gives a remarkably useful handle to generate other functional groups. This transformation can be carried out using a cobalt or rhodium catalyst in a hydrogen/carbon monoxide atmosphere and consists of four stages: metal insertion, migratory insertion, heterolytic cleavage, and ligand exchange. Breit et al. generated extended alkane functionality by hydroformylation, olefination, and then hydrogenation.[6]

Orthogonal tandem catalysis[edit]

Orthogonal tandem catalysis is a "one-pot reaction in which sequential catalytic processes occur through two or more functionally distinct, and preferably non-interfering, catalytic cycles".[7] This technique has been deployed in tandem alkane-dehydrogenation-olefin-metathesis catalysis [8][9]


  1. ^ a b c Concurrent Tandem Catalysis Julia-Christina Wasilke, Stephen J. Obrey, R. Tom Baker, and Guillermo C. Bazan Chemical Reviews 2005 105 (3), 1001-1020 doi:10.1021/cr020018n
  2. ^ Beach, B. L.; Kissin, Y. V. J. Polym. Sci.: Polym. Chem. Ed. 22 (1984) 3027
  3. ^ Barnhart, R. W.; Bazan, G. C. J. Am. Chem. Soc. 120 (1998) 1082
  4. ^ Komon, Z. J. A.; Bu, X.; Bazan, G. C. J. Am. Chem. Soc. 122 (2000) 1830
  5. ^ Cossy, J.; Bargiggia, F.; BouzBouz, S. Org. Lett. 5 (2003) 459
  6. ^ B. Breit, S.K. Zahn Polyhedron 19 (2000) 513
  7. ^ Orthogonal tandem catalysis Tracy L. Lohr and Tobin J. Marks Nature Chemistry 7, 477–482 (2015) doi:10.1038/nchem.2262
  8. ^ Haibach, M. C., Kundu, S., Brookhart, M. & Goldman, A. S. Alkane metathesis by tandem alkane-dehydrogenation-olefin-metathesis catalysis and related chemistry. Acc. Chem. Res. 45, 947–958 (2012). doi:10.1021/ar3000713
  9. ^ Chen, C. Y., O'Rear, D. J. & Leung, P. Molecular redistribution and molecular averaging: disproportionation of paraffins via bifunctional catalysis. Top. Catal. 55, 1344–1361 (2012). doi:10.1007/s11244-012-9910-3