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dc.date.accessioned2016-02-17T06:42:43Z-
dc.date.available2016-02-17T06:42:43Z-
dc.date.issued1979-01-
dc.identifier.urihttp://hdl.handle.net/123456789/3998-
dc.description.abstractA mixture of vapourised acetic acid and 0.25 percent triethyl phosphate is fed into a tubular reactor. Pyrolysis takes place at 7500C under a pressure of 200 mmHg. The cracking furnace exit gases containing acetic anhydride, acetic acid, ketene and water are cooled and condensed. 30-35 percent aqueous acetic acid is withdrawn in a separator. The uncondensed gases of almost pure ketene, are reacted with acetic acid in a series of scrubbers. The conversion of acetic acid is about 90 percent per pass and a selectivity of acetic anhydride based on acetic acid is about 90 percent. Acetic acid is recovered in a raw acetic anhydride column and recycled. Raw acetic anhydride is finished to remove low boilers and tars.en_US
dc.language.isoenen_US
dc.publisherUnited Nations Industrial Development Organizationen_US
dc.subjectAcetic Anhydrideen_US
dc.titleAcetic Anhydrideen_US
dc.typeOtheren_US
Appears in Collections:United Nations Industrial Development Organization

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