Cumene tower is the main device of cumene production unit,using of advanced control strategies based on traditional control scheme,the control system optimizing scheme has been designed for the cumene tower system,cumene tower steam generator system,cumene tower Top system and cumene failed product tank system four-part,and so on.

Bis(tert-butylperoxy) diisopropyl benzene was synthesized from diisopropyl benzene by peroxidation,reduction,synthesis of BIPB.

preparation of p-nitroisopropyl benzene by nitration of isopropyl benzene;

Alkylation of benzene with propylene to isopropyl benzene with ionic liquid as catalyst;

Thermodynamic analysis of diisopropylbenzene transalkylation reaction;

Synthesis of diisopropylbenzene and triisopropylbenzene by heterogeneous catalytic method;

Hβ-1,Hβ-2 and Hβ-3 molecular sieves modified with NH_4NO_3,diammonium citrate and triammonium citrate respectively were characterized by means of XRD,NH_3-TPD and IR,and used as catalysts for diisopropylbenzene(DIPB)isomerization.

Kinetics and mechanism for α-methylstyrene hydrogenation to cumene;

Preparation of cumene by hydrogenation of α-methylstyrene in a trickle-bed reactor;

Flow boiling heat transfer and pressure drop of high saturation temperature organic fluid cumene in vertical tube;

The typical industrial technology of producing phenol was cumene process containing four steps: alkylation,oxidation,purification and recovering.