Hello,
I have a question regarding the configuration of the bypass pressure control valve (PCV) in our combined cycle power plant.
The HRSG bypass PCV is set to override close when the condenser vacuum pressure indicator (PI-0901) exceeds -0.5 Bar.g (-375 mmHg).
Could someone explain why...
Hello,
I have a question regarding the control logic of the HRSG (Heat Recovery Steam Generator) HP (High Pressure) Bypass system.
The current system implements the following logic:
- When the HP Bypass PCV (Pressure Control Valve) opens 95% or more, the pressure setpoint is changed to a value...
If a fuse in one of the three phases breaks before reaching the VT (Voltage Transformer) used for measuring the generator terminal voltage, and this situation is left unattended for a long time, what issues could arise?
I'm curious about the reason for the difference in lube oil tank differential pressure during gas turbine startup and shutdown. During startup, the lube oil tank differential pressure is around 8 inches, but it decreases to 6 inches when stopped. I don't quite understand why there is a...
Our company's BFP (Boiler Feed Pump) functions to suction from the LP (Low Pressure) Drum and send it to the HP (High Pressure) and IP (Intermediate Pressure) drums. When we start the BFP, the HP discharge small MOV (Motor-Operated Valve) opens, then the BFP starts, and after 1 minute, the HP...
I know that it is usually used for self sealing with HP Leak off Steam.
However, in my power plant steam turbine, leak-off re-entry stop valve (LRSV) is open and sends HP Leak off Steam to the Lp Header side.
Why is the hp leak off steam sent as Lp Header instead of using Self Sealing?