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dc.date.accessioned 2016-02-17T06:42:43Z
dc.date.available 2016-02-17T06:42:43Z
dc.date.issued 1979-01
dc.identifier.uri http://hdl.handle.net/123456789/3998
dc.description.abstract A 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acetic anhydride, acetic acid, ketene and water are cooled and condensed. 30-35 percent aqueous acetic acid is withdrawn in a separator.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.iso en en_US
dc.publisher United Nations Industrial Development Organization en_US
dc.subject Acetic Anhydride en_US
dc.title Acetic Anhydride en_US
dc.type Other en_US


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