Transcritical CO2-catalyzed esterification/condensation-separation coupled reaction method and its equipment
A technology of catalytic condensation and coupling reaction, applied in chemical instruments and methods, preparation of organic compounds, preparation of carboxylic acid esters, etc., can solve the problems of product catalyst pollution, low product conversion rate, poor product quality, etc., to improve reaction The effect of speed and balance conversion rate, improving thermal efficiency and reducing exergy loss
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Embodiment 1
[0044] as attached Figure 1-4 As shown, the device for catalyzing esterification / condensation-separation coupled method for preparing rosin ester includes: dissolution kettle 1, esterification / condensation reactor 2, expander 3, gas-liquid separator 4, turbine compressor 5, Alcohol separation tower 6, reflux pump 7.
[0045] The discharge port of the dissolving tank 1 is connected with the feed port of the esterification / condensation reactor 2, and the dissolving tank 1 is used for dissolving raw materials required for production. The esterification / condensation reactor 2 is cylindrical. The upper part of the esterification / condensation reactor is provided with a feed port 21, a gas outlet 22, and the bottom is provided with a discharge port 23. The esterification / condensation reactor 2 includes a heating pipe 24 , is a heating coil, which is located inside the esterification / condensation reactor; a gas distributor 25, which includes an air inlet 251 and a plurality of nozzl...
Embodiment 2
[0051] The reaction apparatus used is the same as in Example 1, a transcritical CO 2 Catalyzed esterification / condensation-separation coupling reaction:
[0052] Add ethylene glycol and cyclohexanone into the melting tank 1 in a molar ratio of 1:0.9, then add 50% turpentine with a mass fraction of ethylene glycol and cyclohexanone, heat and melt to form a mixed material, and feed CO 2 Press the material into the esterification / condensation reactor 2, then raise the temperature to 100°C under stirring, and continuously feed CO 2 To esterification / condensation reactor 2 internal pressure is 5.0Mpa, fill with CO 2 The flow rate is 100m 3 / h, then open the esterification / condensation reactor 2 gas outlet valves to make the small molecule by-product steam, CO produced in the esterification / condensation reaction process 2 The mixed gas phase material flows out continuously, and the outflow volume is less than or equal to 22000m 3 / h, pressure ≤ 20.0MPa, enter gas-liquid separato...
Embodiment 3
[0054] The reaction apparatus used is the same as in Example 1, a transcritical CO 2 Catalyzed esterification / condensation-separation coupling reaction:
[0055] Anhydrous methanol and citral are added into the melting tank 1 at a molar ratio of 1:0.85, and then 10% of the mass fraction of anhydrous methanol and citral is added 2 , heating, melting, forming a mixed material, passing CO 2 Press the material into the esterification / condensation reactor 2, then raise the temperature to 80°C under stirring, and continuously feed CO 2 To the pressure in the esterification / condensation reactor 2 is 8.0Mpa, filled with CO 2 The flow rate is 100m 3 / h, then open the esterification / condensation reactor 2 gas outlet valves to make the small molecule by-product steam, CO produced in the esterification / condensation reaction process 2 The mixed gas phase material flows out continuously, and the outflow volume is less than or equal to 22000m 3 / h, pressure ≤ 20.0MPa, enter gas-liquid s...
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