A kind of preparation method of diisononyl cyclohexane-1,2-dicarboxylate
A technology of diisononyl diformate and cyclohexane, applied in the field of fine chemicals, can solve the problems of shortened reaction time, increased burden on enterprises, high product chromaticity, shortened reaction time, improved production efficiency and yield, Good catalytic activity
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Embodiment 1
[0034] In the reactor, drop into hexahydrophthalic anhydride, isononanol, catalyst acetic anhydride in proportion, wherein: the mol ratio of hexahydrophthalic anhydride and isononanol is 1:2.3, and the acetic anhydride add-on is hexahydrophthalic anhydride quality 5%, heated and stirred under normal pressure, heated to 180 °C and refluxed to start timing, continued to heat up the reaction, maintained at 230 °C for 3 h to obtain material 1, material 1 was the crude product of cyclohexane-1,2-dicarboxylate diisononyl ester ; Pass the material 1 through the falling film evaporator, and flash off excess alcohol under the negative pressure of -0.06MPa, the residence time is 0.002 h, get the material 2, and enter the stripping tank; in the stripping tank, water vapor and Nitrogen bubbling to steam out low molecular weight impurities in material 2 to obtain material 3, which enters the decolorization kettle. The pressure of the stripping tank is controlled at -0.05MPa, the temperatur...
Embodiment 2
[0041] In the reactor, drop into hexahydrophthalic anhydride, isononanol, catalyst acetic anhydride in proportion, wherein: the mol ratio of hexahydrophthalic anhydride and isononanol is 1:2.1, and the acetic anhydride add-on is hexahydrophthalic anhydride quality 2%, heated and stirred under normal pressure, heated to 180 °C and refluxed to start timing, continued to heat up the reaction, maintained at 220 °C for 3 h to obtain material 1, which was the crude product of cyclohexane-1,2-dicarboxylic acid diisononyl ester ; Pass material 1 through a falling film evaporator, and flash off excess alcohol under a negative pressure of -0.08MPa, and the residence time is 0.001 h to obtain material 2, which enters the stripping tank; in the stripping tank, water vapor and Nitrogen bubbling to steam out low molecular weight impurities in material 2 to obtain material 3, which enters the decolorization kettle. The pressure of the stripping tank is controlled at -0.04MPa, the temperature...
Embodiment 3
[0043] In the reactor, drop into hexahydrophthalic anhydride, isononanol, catalyst acetic anhydride in proportion, wherein: the mol ratio of hexahydrophthalic anhydride and isononanol is 1:2.5, and the acetic anhydride add-on is hexahydrophthalic anhydride quality 6%, heated and stirred under normal pressure, heated to 180 °C and refluxed to start timing, continued to heat up the reaction, and maintained at 250 °C for 5 h to obtain material 1. Material 1 was the crude product of cyclohexane-1,2-dicarboxylate diisononyl ester ; Pass material 1 through a falling film evaporator, and flash off excess alcohol under a negative pressure of -0.096MPa, and the residence time is 0.001 h to obtain material 2, which enters the stripping tank; in the stripping tank, water vapor and Nitrogen bubbling to steam out low molecular weight impurities in material 2 to obtain material 3, which enters the decolorization kettle. The pressure of the stripping tank is controlled at -0.08MPa, the tempe...
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