Production of Phenol from Chlorobenzene

Production of Phenol from Chlorobenzene route

Reactions for Production of Phenol

There are three reactions to convert benzene to phenol using chlorination route

 Chlorination

    • Benzene + Cl2 → monochloro benzene
    • Operating temperature: 85°C
    • Catalyst: Fe or FeCl3 catalyst

 Causticization

    • Benzyl chloride + NaOH → sodium benzoate
    • NaOH is in aqueous media
    • Operating conditions: 425°C and 350 atms
    • Exothermic reaction

Hydrolysis

    • Sodium benzoate + HCl (aq) → Phenol + NaCl (aq)
    • Operating conditions: Nothing specific

Production of Phenol Process Flow Diagram

Flow sheet of manufacture of phenol from chlorobenzene route

    Figure. Flow sheet of Production of phenol from chlorobenzene route

    • Benzene is first dried. Dry benzene and FeCl3 catalyst enters the chlorination reactor.
    • After the solid-gas-liquid reaction, the products are further heated up to enter a fractionator.
    • The fractionator separates benzene as a top product and monochloro benzene as the bottom product. The top product also consists of HCl off gas that is obtained as the vapour stream from the partial condenser.
    • The benzene is further cooled and sent back to the reactor and also as a reflux to the fractionator.
    • The bottom product monochloro benzene is mixed with 10% NaOH solution and diphenyl oxide to enter a high pressure pump followed with heat integrated heat exchanger that pre-heats the feed to higher temperature.
    • The feed then enters the causticization reactor which has cooling water tubes to control the temperature.
    • The product stream is cooled using heat integrated exchanger and then enters a neutralizer that is fed with the HCl obtained from the fractionator partial condenser.
    • After neutralization, the product phenol is separated from the aqueous phase using gravity settling principle.
    • The organic layer rich in phenol is sent to a vacuum column to separate the phenol from diphenyl oxide (bottom product). The bottom product is partially recycled to enter the cauticization reactor.

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