A kind of negative ion polymerization solvent refining process
An anion polymerization and solvent refining technology, applied in fractionation and other directions, can solve problems such as solvent CP removal and abnormal polymerization reaction, and achieve the effect of improving product quality and production stability
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0019] SEBS polymerization solvent refining:
[0020] The materials in the tower tank of the light removal tower are returned to the crude tank
[0021] When the feed rate of the dehydration tower is controlled at 20-80t / h, the pressure at the top of the T1 tower is maintained at 0-0.1MPa, the temperature at the top of the T1 tower is stable at 75-100°C, and the temperature at the bottom of the T1 tower is stable at 75-100°C. Dehydration capacity, 15-60t / h of T1 tower bottom component enters T2, T2 pressure control 0.1-0.25MPa, temperature 90-150℃, T2 tower bottom sends part of material to T3 deheavy component through liquid level adjustment, T3 pressure control 0~0.1MPa, temperature 90~120℃, in which the T3 reboiler is advanced before the condensation of the finished product produced by T2, which provides heat source for T3 deweighting and effectively saves steam consumption. After the top component of T1 is condensed, 8-20t / h enters the T4 tower to remove the light componen...
Embodiment 2
[0023] SEBS polymerization solvent refining:
[0024] The material in the tower tank of the light removal tower is returned to the heavy removal tower II
[0025] When the feed of T1 tower is controlled at 20-60t / h, the pressure at the top of T1 tower is maintained at 0-0.1MPa, the temperature at the top of T1 tower is stable at 75-92°C, and the temperature at the bottom of T1 tower is stable at 78-98°C. 15-45t / h of the bottom component of T1 enters T2, the pressure of T2 is controlled at 0.15-0.25MPa, the temperature is 90-140°C, part of the material is sent to the deheavy component of T3 through liquid level adjustment at the bottom of T2, and the pressure of T3 Control 0~0.01MPa, temperature 90~120℃, among them, the T3 reboiler is advanced before the condensation of the finished product extracted from T2, which provides heat source for T3 deweighting and effectively saves steam consumption. After the top component of T1 is condensed, 0~20t / h enters the T4 tower to remove t...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


