Solid base catalyst used for preparing biodiesel by ester interchange and preparation method thereof
A technology of solid base catalyst and biodiesel, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc. It can solve the problems of easy "poisoning, difficult separation, high price, etc., and achieve high stability and The effect of activity, simple process and convenient operation
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Embodiment 1
[0018] Process and steps in the present embodiment are as follows:
[0019] (1) design determines that the composition and weight percentage of solid base catalyst are:
[0020] ZrO2 82%; CaO 16.0%, KOH 2.0%;
[0021] (2) take raw material ZrOCl according to above-mentioned catalyst chemical composition 2 and CaCl 2 , and respectively prepared into solutions with a concentration of 0.1mol / L, put them in a reaction vessel, mix them evenly, and add ammonia water dropwise to the mixed solution under continuous heating and stirring; the heating temperature is 60-70 ℃; the amount of the mixed solution and ammonia water is matched with the molar mass ratio of the two as 1:1; the pH value of the solution is controlled at 8-10 to make it completely precipitate; after the precipitation is complete, let the precipitate age in the mother liquor for 4 hours , then filtered, and the precipitate was repeatedly washed with deionized water to be free of Cl - Detected; then dried at 110°C ...
Embodiment 2
[0026] The processes and steps in this embodiment are exactly the same as those in Embodiment 1 above. The difference is: in (2) step, ZrOCl 2 and CaCl 2 The prepared solution has a concentration of 0.3 mol / L; the roasting temperature used in the roasting process is 650° C., and the roasting time is 4 hours. When preparing biodiesel, the temperature of the transesterification reaction is 140° C., and the reaction time is 4 hours.
[0027] A sample was taken for liquid chromatography detection, and the conversion rate of fatty acid methyl ester was measured to be 87.62%.
Embodiment 3
[0029] The processes and steps in this embodiment are exactly the same as those in Embodiment 1 above. The difference is: the calcination temperature used in the calcination process is 750° C., and the calcination time is 8 hours. When preparing biodiesel, the temperature of the transesterification reaction is 180° C., and the reaction time is 5 hours.
[0030] A sample was taken for liquid chromatography detection, and the conversion rate of fatty acid methyl ester was measured to be 90.22%.
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