Distillation: processes – separatory – With chemical reaction
Patent
1983-10-26
1985-06-11
Smith, William F.
Distillation: processes, separatory
With chemical reaction
203 78, 203 80, 203 84, 585354, 585803, 585832, B01D 314
Patent
active
045226881
ABSTRACT:
The process gives highly pure cyclopentadiene and methylcyclopentadiene from a cracked gasoline fraction. The merit of the process is that cyclopentadiene and methylcyclopentadiene are recovered by adding a simple distillation system to a conventional cracked gasoline treating plant without altering the plant and operating conditions thereof. An internal reflux stream is withdrawn from the stripping section of a BTX column of a conventional cracked gasoline treating plant, and is sent to a depolymerization-distillation column operated at a bottom temperature of 160.degree.-230.degree. C. The overhead stream of the column is sent to a cyclopentadiene column operated at a bottom temperature of 160.degree.-230.degree. C. Cyclopentadiene is recovered from the overhead of the column, and the bottom stream is sent to methylcyclopentadiene column operated at a bottom temperature of 170.degree.-210.degree. C. Methylcyclopentadiene is recovered from the overhead of the column.
REFERENCES:
patent: 2439307 (1948-04-01), Legatski
patent: 2636056 (1953-04-01), Jones
patent: 2733279 (1956-01-01), Wilson et al.
patent: 2733280 (1956-01-01), Hamner
patent: 2813134 (1953-11-01), Johnson
Hosaka Takao
Maruyama Isao
Takahashi Asao
Yokogawa Akira
Maruzen Petrochemical Co. Ltd.
Smith William F.
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