Polytetramethylene ether glycol (PTMEG) depolymerization process
A process and reactor technology, applied in the direction of organic chemistry, etc., can solve the problems of unstable depolymerization discharge, high depolymerization cost, reboiler cleaning, frequent switching, etc.
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Embodiment 1
[0023] The present embodiment provides a kind of PTMEG depolymerization technique, comprises the steps:
[0024] S1. Confirm that the reactor R9101 has been cleaned and emptied, and add steam condensate to the reactor R9101 until the liquid level LT11115 reaches 10% of the tank volume;
[0025] S2. Confirm that the valve between the booster pump P0508B and the reactor R9101 is open, and the electric heat tracing on all pipelines is normally put into use;
[0026] S3. The main control adjusts the steam regulating valve TV11102 of the preheater E9101, controls the temperature of the preheater to 155°C, starts the booster pump P0508B, adjusts the pressure to 6.0bar(G), and preheats the PTMEG defective product in the preheater After reaching 155°C, send it into the reactor R9101;
[0027] S4, when the liquid level in the reactor R9101 reaches 30% of the tank volume, start the circulation pump P9102, and return the PTMEG defective product in the reactor R9101 through the reboiler ...
Embodiment 2
[0034] The present embodiment provides a kind of PTMEG depolymerization technique, comprises the steps:
[0035] S1. Confirm that the reactor R9101 has been cleaned and emptied, and add steam condensate to the reactor R9101 until the liquid level LT11115 reaches 12% of the tank volume;
[0036] S2. Confirm that the valve between the booster pump P0508B and the reactor R9101 is open, and the electric heat tracing on all pipelines is normally put into use;
[0037] S3. The main control adjusts the steam regulating valve TV11102 of the preheater E9101, controls the temperature of the preheater to 150°C, starts the booster pump P0508B, adjusts the pressure to 6.0bar(G), and preheats the PTMEG defective product in the preheater After reaching 150°C, it is sent to the reactor R9101;
[0038] S4, when the liquid level in the reactor R9101 reaches 40% of the tank volume, start the circulation pump P9102, and reflux the PTMEG defective product in the reactor R9101 after the reboiler E...
Embodiment 3
[0045] The present embodiment provides a kind of PTMEG depolymerization technique, comprises the steps:
[0046] S1. Confirm that the reactor R9101 has been cleaned and emptied, and add desalted water to the reactor R9101 until the liquid level LT11115 reaches 10% of the tank volume;
[0047] S2. Confirm that the valve between the booster pump P0508B and the reactor R9101 is open, and the electric heat tracing on all pipelines is normally put into use;
[0048] S3. The main control adjusts the steam regulating valve TV11102 of the preheater E9101, controls the temperature of the preheater to 170°C, starts the booster pump P0508B, adjusts the pressure to 6.0bar(G), and preheats the PTMEG defective product in the preheater After reaching 170°C, it is sent to the reactor R9101;
[0049] S4, when the liquid level in the reactor R9101 reaches 35% of the tank volume, start the circulation pump P9102, and return the defective PTMEG in the reactor R9101 to the reboiler E9102B, and co...
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