This study of β-caryophyllene hydration to produce
β-caryophyllene alcohol was carried out catalyzed by strong
acidic cation exchange resin NKC-9. The effects of different parameters
such as agitation speed, catalyst type, catalyst loading, mass ratio
of the reactants, temperature, and reaction time on the conversion
of β-caryophyllene and yield of β-caryophyllene alcohol
in a stirred-tank reactor have been investigated to obtain the optimal
conditions. Under the optimal conditions (catalyst loading 20%(w/w), nβ‑caryophyllene/nwater 1/1, reaction temperature 363.15 K, reaction time
30–40 min), the experiment was then carried out in a pilot-scale
stirred tank reactor and in a novel pilot-scale jet reactor respectively
to achieve excellent performance. The β-caryophyllene alcohol
has been purified by rectifying column and recrystallized. A pseudohomogeneous
(PH) model was used to correlate the kinetic data in the temperature
range from 333.15 to 363.15 K. The estimated kinetic parameters make
the calculated results in excellent agreement with the experimental
results.