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“Coking is a refinery unit operation that upgrades material called bottoms from the atmospheric or vacuum distillation column into higher-value products and produces petroleum coke—a coal-like material.” [1]. In heterogeneous catalysis, the process is undesirable because the clinker blocks the catalytic sites. Coking is characteristic of high temperature reactions involving hydrocarbons feedstocks. Typically coking is reversed by combustion, provided that the catalyst will tolerate such.[2]

A simplified equation for coking is shown in the case of ethylene:

3 C2H4 → 2 C ("coke") + 2 C2H6

A more realistic but complex view involves the alkylation of an aromatic ring of a coke nucleus. Acidic catalysts are thus especially prone to coking because they are effective at generating carbocations (i.e., alkylating agents).

Coking is one of several mechanisms for the deactivation of a heterogeneous catalyst. Other mechanisms include sintering, poisoning, and solid-state transformation of the catalyst.[3][4]

ReferencesEdit

  1. ^ Template:Cite website=
  2. ^ H. Schultz. ""Coking" of zeolites during methanol conversion: Basic reactions of the MTO-, MTP- and MTG processes". Catalysis Today. 154: 183–194. doi:10.1016/j.cattod.2010.05.012.
  3. ^ Forzatti, P.; Lietti, L. (1999). "Catalyst Deactivation". Catalysis Today. 52: 165–181. doi:10.1016/S0920-5861(99)00074-7.CS1 maint: uses authors parameter (link)
  4. ^ Bartholomew, Calvin H (2001). "Mechanisms of Catalyst Deactivation". Applied Catalysis A: General. 212 (1–2): 17–60. doi:10.1016/S0926-860X(00)00843-7.