Benzene → Nitrobenzene

HRID 623348Notes

Reaction equation

HRID 623348 reaction equation
S(=O)(=O)(O)O.[N+:6]([O-:9])(O)=[O:7].[CH:10]1[CH:15]=[CH:14][CH:13]=[CH:12][CH:11]=1>>[N+:6]([C:10]1[CH:15]=[CH:14][CH:13]=[CH:12][CH:11]=1)([O-:9])=[O:7]

Participants

4

Procedure

A stream of sulfuric acid into which first a stream of nitric acid and then a combined stream of fresh benzene and recycled benzene were metered is fed to a reactor. The residence time between the addition of nitric acid to the sulfuric acid and the entry of the nitrating solution into the reactor is less than 10 seconds. 6% of recycled benzene are used as excess benzene. After complete reaction of the nitric acid with the benzene to give nitrobenzene under an adiabatic reaction procedure, the now approx. 130° C. hot reaction product is fed to a phase separation apparatus in which the reaction product breaks down into an organic phase (=crude nitrobenzene, also comprising benzene in addition to nitrobenzene) and an aqueous phase (=waste acid, also comprising small contents of nitrobenzene and benzene in addition to sulfuric acid). The aqueous phase mainly encompassing sulfuric acid is subjected to a flash evaporation of water in an evaporator by sudden pressure reduction and is concentrated in this manner. The concentrated sulfuric acid is temporarily stored in a sulfuric acid reservoir tank to be used again in the nitration. After the crude nitrobenzene has been separated off in the phase separation apparatus, it is cooled to approx. 40° C. to 50° C. in a crude nitrobenzene cooler and fed to a wash for work-up. The purified nitrobenzene stream thus obtained, which has been largely freed from nitrophenols and salts is reheated and freed from water and benzene, which are separated off overhead, in a rectification column, as a result of which dried pure nitrobenzene is obtained in the bottom of the column. The condensed head product of the rectification column is fed to a phase separation apparatus in which the head product breaks down into an organic phase (comprising benzene) and an aqueous phase. The benzene is stored temporarily in a buffer tank and from there is returned as recycle benzene into the inlet of the reactor for reaction, as already described above.

Workup

  1. waitthe entry of the nitrating solution into the reactor is less than 10 seconds

Sources & evidence

ORD record
ord-ed92c5e7340645539b1d18a5d5e8ffe0
Source dataset
uspto-grants-2016_04
Patent number
US09302978B1

Reaction notes

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