Liquid phase transalkylation of benzene with poly-isopropylbenzene(PIPB,diisopropylbenzene and triisopropylbenzene)was studied over MP-02 catalyst in a 50 mL fixed bed reactor,and effects of various parameters,such as reaction temperature,space velocity of PIPB and mass ratio of benzene to PIPB,were investigated.

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.