dadams
Chemical
- Jun 28, 2007
- 2
ANSI
Vertical
Inline Pump
FlowServe 2K2X10 10 Hp
Temp < 200 deg F
Disch pressure < 75 psig
3600 rpm
Any tips on mounting or support of pump and associated piping?
I have heard the motor will develop a gyroscopic effect and create a strong overturning moment.
Is it better to left pump float with pipe and let pipe restrict the overturning moment or
Fix the pump and fix the pipe at the suc/dschg connections?
Pipe operates at low temp, 2" dia, bends/elbows in horizontal plane in pipe on both ends within 10 ft.
Manufacturer info says you could do either. Just keep within allowable limits. I don't have resources to do pipe stress calcs now nor do I want to on low temp 2" pipe.
Any rule of thumb tips?
Vertical
Inline Pump
FlowServe 2K2X10 10 Hp
Temp < 200 deg F
Disch pressure < 75 psig
3600 rpm
Any tips on mounting or support of pump and associated piping?
I have heard the motor will develop a gyroscopic effect and create a strong overturning moment.
Is it better to left pump float with pipe and let pipe restrict the overturning moment or
Fix the pump and fix the pipe at the suc/dschg connections?
Pipe operates at low temp, 2" dia, bends/elbows in horizontal plane in pipe on both ends within 10 ft.
Manufacturer info says you could do either. Just keep within allowable limits. I don't have resources to do pipe stress calcs now nor do I want to on low temp 2" pipe.
Any rule of thumb tips?
