Control method of sewage discharge and recovery for high-boiling tower of vinyl chloride
A control method and high-boiling tower technology, applied in the direction of distillation adjustment/control, disproportionation separation/purification of halogenated hydrocarbons, organic chemistry, etc., can solve the problems of random manual operation, site abnormality, frequent operation, etc., to overcome the problem of product The impact of quality and safe production, the improvement of control accuracy and detection accuracy, and the effect of improving safety and stability
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Embodiment 2
[0056] The difference between embodiment 2 and embodiment 1 is: the central control operation of DCS control program [manual] and [automatic], [start], [stop] and [pause] of high boiling tower 2 [drainage] and [recovery] are added Select the button and switch button, the operator can perform [Automatic] and [Start] on the central control operation station to select the linkage operation according to the actual situation on site, or pause or stop the step according to the timely production situation, click [Stop] and then proceed to [Manual 】The valve can be switched on and off during program control implementation.
Embodiment 3
[0057] Embodiment 3 differs from Embodiment 1 in that it is a control method for blowdown and recovery of vinyl chloride high-boiling towers, a newly added on-site operation control panel 21 in the process of blowdown→liquid intake→distillation→recovery→filling, Newly added manual control button 22, automatic control button 23, step-by-step control button 33, linkage control button 34, start control button 35, stop control button 36, pause control button 37, sewage control button 38, liquid inlet control button 39, Distillation control button 40, recovery control button 41, filling control button 42; newly added high boiling tower blowdown valve start and stop control 24, distillation three tower kettle hot water valve start and stop control 25, distillation three tower liquid inlet valve start and stop Control 26, start and stop control of monomer recovery valve of the third distillation tower 27, start and stop control of the circulation reflux valve of the third distillation...
Embodiment 4
[0058] The difference between embodiment 4 and embodiment 1 is that the DCS controls the internal switching value, and the internal switch and valve position start and reset procedures are newly added. Its function is to discharge sewage in the process of automatic operation of all programs→liquid intake→distillation→recovery→ At the end of filling, reset all internal switches and valve positions to the initial state, and finally enter the initial standby stage.
[0059] In the above embodiments, the preset time and liquid level reference values can be multiple based on experience, and the specific values are extremely important to the size, reaction characteristics, and production indicators of the high boiling tower, raffinate storage tank, and three distillation towers. .
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