Method for recovering heat integrated solvent in continuous production of toluene di-isocyanate
A technology of toluene diisocyanate and recovery method, which is applied in the direction of purification/separation of isocyanic acid derivatives, climate sustainability, sustainable manufacturing/processing, etc., can solve the problem of a large amount of materials to be processed, reduce heat consumption, reduce Production cost and energy consumption reduction effect
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Embodiment 1
[0052] Recovery method of solvent o-dichlorobenzene in the continuous production of toluene diisocyanate without heat integration:
[0053] The material to be distilled that comprises toluene diisocyanate and inert organic solvent comes from hydrogen chloride stripping section, and flow rate is 96100kg / hr, 180 ℃ of temperature, absolute pressure 380kPa, and wherein o-dichlorobenzene (ODCB) mass content is 91.6%, toluene diisocyanate ( TDI) mass content is 7.8%, also has a small amount of phosgene, carbon tetrachloride and tar in addition. The material to be distilled passes through a two-stage solvent removal tower to remove the solvent. The first solvent removal tower is a packed tower with a theoretical plate number of 30. It is operated at an absolute pressure of 18kPa at the top of the tower. The side line extracts pure ODCB at 76400kg / hr, wherein the TDI content is less than 27ppb (mass fraction), and the phosgene content is less than 2ppm (mass fraction). The steam at th...
Embodiment 2
[0057] Embodiment 2 is a heat-integrated solvent recovery method in the continuous production of toluene diisocyanate.
[0058] The material to be distilled comprising toluene diisocyanate and an inert organic solvent is the same as in Example 1.
[0059] The material to be distilled comprising toluene diisocyanate and an inert organic solvent is exchanged with the crude product at the outlet of the phosgenation reactor with a flow rate of 151906kg / hr, and the temperature of the material to be distilled after the heat exchange is reduced to 120°C. The ratio of % will divide the material to be distilled after the heat exchange into two parts, and distill as the feedstock of the first solvent removal tower (solvent is o-dichlorobenzene (ODCB)) and the second solvent removal tower respectively, and the first solvent removal tower The removal tower is a packed tower with a theoretical plate number of 30, operated at an absolute pressure of 21kPa at the top of the tower, and the ab...
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