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Hydration of isobutene in liquid‐full and trickle‐bed reactors
Author(s) -
Leung Pak,
Zorrilla C.,
Recasens F.,
Smith J. M.
Publication year - 1986
Publication title -
aiche journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.958
H-Index - 167
eISSN - 1547-5905
pISSN - 0001-1541
DOI - 10.1002/aic.690321109
Subject(s) - trickle bed reactor , chemistry , trickle , mass transfer , catalysis , diffusion , particle (ecology) , kinetics , chemical engineering , atmospheric pressure , particle size , activation energy , chromatography , analytical chemistry (journal) , thermodynamics , organic chemistry , physics , oceanography , engineering , quantum mechanics , political science , law , geology
Rates of hydration of isobutene were measured with Amberlyst‐15 catalyst particles in a differential, liquid‐full recycle reactor operating at atmospheric pressure and 303 to 333 K. Catalysts pretreated in two different ways were studied. Liquid‐to‐particle mass transfer had a small but measurable effect on the rate. Intraparticle diffusion was more significant, as indicated by effectiveness factors from 0.26 for the larger catalyst particles ( d p = 1.04 × 10 −3 m) at 333 K to 0.84 for the smaller particles ( d p = 0.45 × 10 −3 m) at 303 K. The intrinsic rate was first‐order in isobutene concentration with an activation energy of 67 kJ/mol. The intraparticle diffusion resistance is due to the macropores surrounding the very small gel‐type microparticles of which the particles were composed. Some data were obtained for reaction rates in trickle‐bed operation. Global rates were somewhat lower in the trickle‐bed operation than in the liquid‐full runs. Using the previously determined intrinsic kinetics and effectiveness factors, the liquid‐to‐particle mass transfer coefficients could be approximated for the trickle‐bed operation.