Method for regenerating resin in isopropanol recovery process
A technology of resin regeneration and isopropanol, applied in separation methods, filter regeneration, chemical instruments and methods, etc., can solve the problems of high-temperature regeneration of activated carbon, difficult treatment, secondary pollution, etc., and achieve high economic and environmental benefits , Increase the number of cycles and prolong the cycle life
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Embodiment 1
[0070] The present embodiment provides a kind of method that reclaims resin regeneration in the isopropanol process, and described method comprises the steps:
[0071] (A) Utilize the first crude isopropanol after pretreatment to carry out solvent regeneration to the macroporous resin after adsorption (the column height of the model is XDA experimental packing is 30cm, and the density of macroporous resin is 1.2g / mL), The temperature of described solvent regeneration is 40 ℃, and the flow rate of the first crude isopropanol is 1BV / h, and the consumption of the first crude isopropanol is 2 times of resin volume; The quality of isopropanol in the first crude isopropanol The percentage content is 60wt%;
[0072] (B) Using steam to regenerate the macroporous resin after the solvent regeneration in step (A), the temperature of the steam regeneration is 130° C., the quality of the steam is 3 kg, and the pressure is 0.3 kPa.
Embodiment 2
[0074] The present embodiment provides a kind of method that reclaims resin regeneration in the isopropanol process, and described method comprises the steps:
[0075] (A) Utilize the first crude isopropanol after pretreatment to carry out solvent regeneration to the macroporous resin after adsorption (the column height of the model is XDA experimental packing is 32cm, and the density of macroporous resin is 1.2g / mL), The temperature of the solvent regeneration is 5°C, the flow rate of the first crude isopropanol is 0.5BV / h, and the amount of the first crude isopropanol is 3 times of the volume of the resin;
[0076] (B) Using steam to regenerate the macroporous resin after solvent regeneration in step (A), the temperature of the steam regeneration is 180° C., the quality of the steam is 4 kg, and the pressure is 0.4 kPa.
Embodiment 3
[0078] The present embodiment provides a kind of method that reclaims resin regeneration in the isopropanol process, and described method comprises the steps:
[0079] (A) Utilize the first crude isopropanol after the pretreatment to carry out solvent regeneration to the macroporous resin after the adsorption (the column height of the model is XDA experimental packing is 28cm, and the density of the macroporous resin is 1.2g / mL), The temperature for solvent regeneration is 45°C, the flow rate of the first crude isopropanol is 2BV / h, and the amount of the first crude isopropanol is 0.5 times the volume of the resin;
[0080] (B) Using steam to regenerate the macroporous resin after the solvent regeneration in step (A), the temperature of the steam regeneration is 120° C., the quality of the steam is 2 kg, and the pressure is 0.2 kPa.
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