Dilute acetic acid (AA) streams (4.5–15%, w/w) were used in an extractive esterification with 2-ethyl-1-hexanol, exploiting the different solubilities of acetic acid and acetic ester in water. The main advantage of the process is the simultaneous water purification and production of an ester having a good commercial value. The new method proposed has the purposes to save the costs arising from the treatment of the waste water and utilize in chemical synthesis the acetic acid otherwise eliminated. The performed reaction is a three-phase system which Amberlyst 15 was used as acid catalyst in. It was clearly demonstrated that the reaction takes place in the organic phase and not in the aqueous one and a conversion of about 70% can be reached. A simplified mathematical model was also proposed.

Increasing the value of dilute acetic acid streams through esterification: Part I. Experimental analysis of the reaction zone / V. Ragaini, C.L.M. Bianchi, C. Pirola, G. Carvoli. - In: APPLIED CATALYSIS. B, ENVIRONMENTAL. - ISSN 0926-3373. - 64:1-2(2006), pp. 66-71.

Increasing the value of dilute acetic acid streams through esterification: Part I. Experimental analysis of the reaction zone

V. Ragaini
Primo
;
C.L.M. Bianchi
Secondo
;
C. Pirola
Penultimo
;
2006

Abstract

Dilute acetic acid (AA) streams (4.5–15%, w/w) were used in an extractive esterification with 2-ethyl-1-hexanol, exploiting the different solubilities of acetic acid and acetic ester in water. The main advantage of the process is the simultaneous water purification and production of an ester having a good commercial value. The new method proposed has the purposes to save the costs arising from the treatment of the waste water and utilize in chemical synthesis the acetic acid otherwise eliminated. The performed reaction is a three-phase system which Amberlyst 15 was used as acid catalyst in. It was clearly demonstrated that the reaction takes place in the organic phase and not in the aqueous one and a conversion of about 70% can be reached. A simplified mathematical model was also proposed.
Acetic acid recovery; Esterification reaction; Extractive esterification; Mathematical model; Water purification
Settore ING-IND/23 - Chimica Fisica Applicata
Settore ING-IND/25 - Impianti Chimici
2006
http://scienceserver.cilea.it/cgi-bin/sciserv.pl?collection=journals&journal=09263373&issue=v64i1-2&article=66_itvodaaste&form=fulltext
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2434/28858
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