DanielWW
Mechanical
- Sep 9, 2013
- 10
I've been tasked with doing an initial investigation into a possible new arrangement for a trip and throttle (T&T) valve system for a steam turbine. The T&T valve has a spring which is held open with oil pressurized to 80psi. If the turbine overspeeds, a solenoid valve opens, depressurizing the system and shutting the trip and throttle valve when pressure at the spring reaches 50psi. Normally, each trip and throttle valve has its own solenoid valve located close to the trip and throttle valve. The question that came from a customer is: can we use a single solenoid valve to operate two trip and throttle valves.
The main concern is that by increasing the length of pipe from the solenoid valve to the T&T valve, we could delay the closing of the T&T valve because the pressure wave would take longer to get there. Some engineers I've talked to don't think this would be a problem because the pressure wave will travel at the speed of sound, adding only a negligible delay to the closing of the valve (which normally takes around .450 seconds to close from the time the governor sends the overspeed signal and the spring slams the valve shut). However, another engineer recommends calculating the pressure change as a function of time at different points in the system.
So my main questions are:
1. Is it possible/necessary to calculate the pressure decay over time due to the rapid opening of a solenoid valve?
2. Are there any other concerns with this design that I may be overlooking?
Thanks!
The main concern is that by increasing the length of pipe from the solenoid valve to the T&T valve, we could delay the closing of the T&T valve because the pressure wave would take longer to get there. Some engineers I've talked to don't think this would be a problem because the pressure wave will travel at the speed of sound, adding only a negligible delay to the closing of the valve (which normally takes around .450 seconds to close from the time the governor sends the overspeed signal and the spring slams the valve shut). However, another engineer recommends calculating the pressure change as a function of time at different points in the system.
So my main questions are:
1. Is it possible/necessary to calculate the pressure decay over time due to the rapid opening of a solenoid valve?
2. Are there any other concerns with this design that I may be overlooking?
Thanks!