Cumene process

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The cumene process (cumene-phenol process, Hock process) is an

industrial process for synthesizing phenol and acetone from benzene and propylene. The term stems from cumene (isopropyl benzene), the intermediate material during the process. It was invented by R. Ūdris and P. Sergeyev in 1942 (USSR),[1] and independently by Heinrich Hock in 1944.[2][3]

This process converts two relatively cheap starting materials, benzene and propylene, into two more valuable ones, phenol and acetone. Other reactants required are oxygen from air and small amounts of a radical initiator. Most of the worldwide production of phenol and acetone is now based on this method. In 2022, nearly 10.8 million tonnes of phenol was produced by the cumene process.[4] In order for this process to be economical, there must also be demand for the acetone by-product as well as the phenol.[5]

First stage of Hock process: alkylation of benzene with propylene.
Second stage of Hock process: autoxidation of cumene.

Steps of the process

Cumene is formed in the gas-phase

benzylic hydrogen from cumene and hence forms a cumene radical
:

The cumene radical then

atm
is used to ensure that the unstable peroxide is kept in liquid state.

Cumene hydroperoxide undergoes a rearrangement reaction in an acidic medium (the Hock rearrangement) to give phenol and acetone. In the first step, the terminal hydroperoxy oxygen atom is protonated. This is followed by a step in which the phenyl group migrates from the benzyl carbon to the adjacent oxygen and a water molecule is lost, producing a resonance stabilized tertiary carbocation. The concerted mechanism of this step is similar to the mechanisms of the Baeyer–Villiger oxidation[6] and Criegee rearrangement reactions, and also the oxidation step of the hydroboration–oxidation process.[7] In 2009, an acidified bentonite clay was proven to be a more economical catalyst than sulfuric acid as the acid medium.

The resulting carbocation is then attacked by water, forming a hemiacetal-like structure. After transfer of a proton from the hydroxy oxygen to the ether oxygen, the ion falls apart into phenol and acetone.

Related reactions and modifications

Alternatives to acetone co-production

Cyclohexylbenzene can replace isopropylbenzene. Via the Hock rearrangement, cyclohexylbenzene hydroperoxide cleaves to give phenol and cyclohexanone. Cyclohexanone is an important precursor to some nylons.[8]

Starting with the alkylation of benzene with mixture of

2-butenes, the cumene process produces phenol and butanones.[5]

Alternatives to phenol production

Acetone processing

Crude acetone is hydrogenated in the liquid phase over Raney nickel or a mixture of copper and chromium oxide to give isopropyl alcohol. This process is useful, when it is coupled with excess acetone production.[14]

isopropanol product to propene, which is recycled as a starting reactant.[5]

Byproducts

Byproducts of the cumene process to produce phenol and acetone are

alpha-methylstyrene
.

See also

References

  1. ^ "Latvian". Archived from the original on 2016-03-03. Retrieved 2011-02-27.
  2. ^ Concise Encyclopedia Chemistry (1993) Mary Eagleso
  3. ^ "Phenol Market Size, Share, Analysis & Forecast, 2035 – ChemAnalyst". ChemAnalyst. Retrieved 2024-04-09.
  4. ^ a b c "Direct Routes to Phenol". Archived from the original on 2007-04-09. Retrieved 2006-12-26.
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  6. .
  7. ^ Plotkin, Jeffrey S. (2016-03-21). "What's New in Phenol Production?". American Chemical Society. Archived from the original on 2019-10-27. Retrieved 2018-01-02.
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External links