kts5313
Chemical
- Mar 22, 2024
- 1
Hi,
The pressure build circuit in my situation is as follows: We have two LIN tanks (15,000 gallons each) that share a common ambient pressure build vaporizer (PBU,PBV), the LIN is drawn from the tanks to the vaporizer and the GAN is fed back to the tanks to maintain tank pressure. The pressure build vaporizer controls the pressure in the tanks around 130 psig through a pneumatic control valve on the outlet of the vaporizer.
Under normal operating conditions, the tanks feed about 5000 lb/hr combined (to the plant as well as the PBU). For this reason, LIN deliveries occur twice a day (~ every 12 hours). When the LIN is delivered, the pressure in the tanks naturally drop. The pressure build vaporizer tries to correct for this using the control valve (Cv=20) to build the pressure back to setpoint, but often overshoots. The pressure build vaporizer was recently replaced with a larger unit capable of handling 35K SCFH, which is oversized 1.5x for the plant demand. The issue is ice build up. The PBU is continuously covered in ice, and in the winter it is a hazard. I believe the issue is the deliveries and how often they occur as the control valve sees the drop in pressure and allows the LIN to flog through excessively in an attempt to build the tank pressure back up. My thought currently is to modify the control valve either by reducing the instrument air pressure signal to the controller or change the control valve seat to reduce the Cv.
I do not have much experience in this particular situation so I was wondering if anyone else has experienced something similar? Is this the nature of the process or is there something that can be done to reduce ice buildup on the vaporizer? Any help would be greatly appreciated, I can provide more details if needed. I attached a basic diagram for reference.
The pressure build circuit in my situation is as follows: We have two LIN tanks (15,000 gallons each) that share a common ambient pressure build vaporizer (PBU,PBV), the LIN is drawn from the tanks to the vaporizer and the GAN is fed back to the tanks to maintain tank pressure. The pressure build vaporizer controls the pressure in the tanks around 130 psig through a pneumatic control valve on the outlet of the vaporizer.
Under normal operating conditions, the tanks feed about 5000 lb/hr combined (to the plant as well as the PBU). For this reason, LIN deliveries occur twice a day (~ every 12 hours). When the LIN is delivered, the pressure in the tanks naturally drop. The pressure build vaporizer tries to correct for this using the control valve (Cv=20) to build the pressure back to setpoint, but often overshoots. The pressure build vaporizer was recently replaced with a larger unit capable of handling 35K SCFH, which is oversized 1.5x for the plant demand. The issue is ice build up. The PBU is continuously covered in ice, and in the winter it is a hazard. I believe the issue is the deliveries and how often they occur as the control valve sees the drop in pressure and allows the LIN to flog through excessively in an attempt to build the tank pressure back up. My thought currently is to modify the control valve either by reducing the instrument air pressure signal to the controller or change the control valve seat to reduce the Cv.
I do not have much experience in this particular situation so I was wondering if anyone else has experienced something similar? Is this the nature of the process or is there something that can be done to reduce ice buildup on the vaporizer? Any help would be greatly appreciated, I can provide more details if needed. I attached a basic diagram for reference.