mb73
Mechanical
- Jan 13, 2003
- 9
I am new to this forum and just wanted to start a discussion on allowable steam flow velocities in reheat steam piping.
Crane No.410 gives an acceptable upper limit as 20,000 fpm. However, I am interested in the basis for this. Is it because of the pressure drop associated with this, noise, shock formation, scale removal,creation of high vortices around thermocouples in the piping???
And secondly, how reactive is the IP turbine to pressure drops beyond design.? For example, if at full load, the reheat stop valves see 500 psig and there is an increase in upstream piping size resulting in a pressure of 490 e.g. how would that impact turbine performance?
Looking forward to your responses.
Crane No.410 gives an acceptable upper limit as 20,000 fpm. However, I am interested in the basis for this. Is it because of the pressure drop associated with this, noise, shock formation, scale removal,creation of high vortices around thermocouples in the piping???
And secondly, how reactive is the IP turbine to pressure drops beyond design.? For example, if at full load, the reheat stop valves see 500 psig and there is an increase in upstream piping size resulting in a pressure of 490 e.g. how would that impact turbine performance?
Looking forward to your responses.