. Gas-liquid-liquid reaction engineering: the Koch synthesis of pivalic acid from iso-and tert-butanol; Reaction kinetics and the effect of a dispersed second-liquid phase. Chemical Engineering Science, 54(21), 4801-4809. https://doi.org/10.1016/S0009-2509(99)00197-9 Copyright Other than for strictly personal use, it is not permitted to download or to forward/distribute the text or part of it without the consent of the author(s) and/or copyright holder(s), unless the work is under an open content license (like Creative Commons).Take-down policy If you believe that this document breaches copyright please contact us providing details, and we will remove access to the work immediately and investigate your claim.Downloaded from the University of Groningen/UMCG research database (Pure): http://www.rug.nl/research/portal. For technical reasons the number of authors shown on this cover page is limited to 10 maximum.
AbstractIn gas}liquid}liquid reaction systems with fast parallel and consecutive reactions the e!ects of mass transfer and mixing on the product yield can be signi"cant. The Koch synthesis of pivalic acid, using sulfuric acid as catalyst, was chosen to study these e!ects. Reaction kinetics and the e!ect of the catalyst-phase composition have been investigated by using isobutanol as reactant. For studying the e!ect of an immiscible liquid phase on the reaction products obtained, the more reactive tert-butanol was used. Pivalic acid can be produced from isobutanol using sulfuric acid as a catalyst solution with 2-methylbutanoic acid as main byproduct, if gas}liquid mass transfer limitations are excluded. The selectivity towards 2-methylbutanoic acid is generally less than 20% and decreases strongly with decreasing acidity. The reaction is "rst order in isobutanol and dehydration is likely to be rate determining. The presence of pivalic acid and isobutanol strongly reduces the apparent reaction rate constant by decreasing the solution acidity (Ho). For the industrially applied backmixed reactors in the Koch synthesis, this may imply that these operate at much lower values for Ho. On addition of an immiscible heptane phase, the reaction products are extracted to some extent and this adds to maintaining a high catalyst solution acidity. Using tert-butanol, the yield and pivalic acid selectivity was found to depend strongly on CO transport to the reaction zone through gas}liquid mass transfer and mixing. The presence of an immiscible heptane phase increased the product yield and selectivity towards pivalic acid signi"cantly.