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[1] Wang H.X., Wu C. M., Bu X. W., Tang W. L., Li L., Qiu T. A benign preparation of sec-butanol via transesterification from sec-butyl acetate using the acidic Imidazolium ionic liquids as catalysts. Chemical Engineering Journal, 246, pp366-372, 2014. [2] Wang H. X., Bu X.W., Huang Z.X., Yang J.B., Qiu T., Synthesis of methacrylic anhydride by batch reactive distillation: reaction kinetics and process. Ind. Eng. Chem. Res, 53(44), pp17317-17324, 2014. [3] Wang H. X., Li L., Ye C. S., Isobaric vapor–liquid equilibria of the binary system acetone + acetone oxime methyl ether at 101.3 kPa, Fluid Phase Equilibria, 342(1) , pp 42-46, 2013. [4] Wang H. X., Xiao J. J., Shen Y. Y., Ye C. S., Li L., Qiu T., Experimental measurements of vapor - liquid equilibrium data for the binary systems of methanol + 2-butyl acetate, 2-butyl alcohol + 2-butyl acetate and methyl acetate + 2-butyl acetate at 101.33 kPa, Journal of Chemical Engineering Data,58(6), pp1827-1832, 2013. [5] Wang H. X., Xiao J. J., Shen Y. Y., Ye C. S., Li L., Qiu T., Reply to Comments on "Experimental measurements of vapor-liquid equilibrium data for the binary systems of methanol + 2-butyl acetate, 2-butyl alcohol + 2-butyl acetate and methyl acetate + 2-butyl acetate at 101.33 kPa", Journal of Chemical Engineering Data,58(12), pp3567-3568, 2013. [6] Wang H. X, Li L., Ye, C. S., Isobaric vapor–liquid equilibria of the binary system acetone+ acetone oxime methyl ether at 101.3 kPa. Fluid Phase Equilibria, 342, pp42-46, 2013 [7] Huang, Z. X., Jiang H. M., Li, L., Wang, H. X, Qiu, T. Density, viscosity, and saturated vapor pressure of ethyl trifluoroacetate. The Journal of Chemical Thermodynamics, 86, pp75-79, 2015 [8] Ye C. S., Wang H. X., Huang G. Q., Qiu T., Adsorption and desorption of DMF on macroporous resin NKA-II in the fixed bed, Chemical Engineering Research and Design, 91(12), pp2713-2720, 2013