TY - JOUR
T1 - Impurity distribution behavior in caprolactam extraction with environmentally benign mixed solvents
AU - Delden, van, M.L.
AU - Drumm, C.
AU - Kuipers, N.J.M.
AU - Haan, de, A.B.
PY - 2006
Y1 - 2006
N2 - In a previous study a solvent mixture of heptane containing 40 mass % heptanol was selected as an alternative in the industrial extraction of caprolactam to replace benzene, toluene, or chlorinated hydrocarbons. This work reports the equilibrium distribution ratio of caprolactam and four model impurities of organic nature, namely, cyclohexanone, aniline, n-methylcaprolactam, and cyclohexane-carboxamide, comparing the mixed solvents with toluene as a reference. The resulting phase equilibria were interpreted using the equilibrium stage model. Based on these calculations it was found that, compared to toluene, the co-extracted fraction of cyclohexanone and aniline was higher, that of n-methylcaprolactam was comparable, and that of cyclohexane-carboxamide was lower using the mixed solvent. Overall, the mixed solvent reduced the fraction of co-extracted impurities by almost 10 %.
AB - In a previous study a solvent mixture of heptane containing 40 mass % heptanol was selected as an alternative in the industrial extraction of caprolactam to replace benzene, toluene, or chlorinated hydrocarbons. This work reports the equilibrium distribution ratio of caprolactam and four model impurities of organic nature, namely, cyclohexanone, aniline, n-methylcaprolactam, and cyclohexane-carboxamide, comparing the mixed solvents with toluene as a reference. The resulting phase equilibria were interpreted using the equilibrium stage model. Based on these calculations it was found that, compared to toluene, the co-extracted fraction of cyclohexanone and aniline was higher, that of n-methylcaprolactam was comparable, and that of cyclohexane-carboxamide was lower using the mixed solvent. Overall, the mixed solvent reduced the fraction of co-extracted impurities by almost 10 %.
U2 - 10.1002/ceat.200600165
DO - 10.1002/ceat.200600165
M3 - Article
SN - 0930-7516
VL - 29
SP - 1221
EP - 1226
JO - Chemical Engineering & Technology
JF - Chemical Engineering & Technology
IS - 10
ER -