chemks2012
Chemical
- May 15, 2013
- 125
Dear all,
I need your help please.
Currently we have high pressure boiler (to generate saturated steam at 60barg, 2000kg/hr) feed pumps with the below stated configuration.
The boiler feed water pumps are high pressure PD pumps (duty and standby) on inverters with the operation pressure of 70barg and 2400kg/hr (max pressure of 80barg, 3000kg/hr at max speed).
The suction side of these PD pumps are connected with a centrifugal booster pump with differential head of 30m, 3m3/hr.
We have a manual block and bleed globe valve arrangement at the suction and discharge of PD pumps.
Currently we cannot achieve required pressure (70barg) and flowrate (2400kg/hr) at the discharge of PD pump and we want to replace those globe valves with full bore (straight through) valves to reduce the pressure drop and hence possible cavitation.
My queries:
1) we are planning to replace suction side globe valves with the ball valves. Do you think ball valves should be ok as the suction side pressure pressure is very low (30m head = 3barg)? Please suggest.
2) we are planning to replace discharge side globe valves with the gate valves? Can we use gate valves for the high pressure lines as high as 70barg? Please comment.
Thanks for your help in advance.
KS
I need your help please.
Currently we have high pressure boiler (to generate saturated steam at 60barg, 2000kg/hr) feed pumps with the below stated configuration.
The boiler feed water pumps are high pressure PD pumps (duty and standby) on inverters with the operation pressure of 70barg and 2400kg/hr (max pressure of 80barg, 3000kg/hr at max speed).
The suction side of these PD pumps are connected with a centrifugal booster pump with differential head of 30m, 3m3/hr.
We have a manual block and bleed globe valve arrangement at the suction and discharge of PD pumps.
Currently we cannot achieve required pressure (70barg) and flowrate (2400kg/hr) at the discharge of PD pump and we want to replace those globe valves with full bore (straight through) valves to reduce the pressure drop and hence possible cavitation.
My queries:
1) we are planning to replace suction side globe valves with the ball valves. Do you think ball valves should be ok as the suction side pressure pressure is very low (30m head = 3barg)? Please suggest.
2) we are planning to replace discharge side globe valves with the gate valves? Can we use gate valves for the high pressure lines as high as 70barg? Please comment.
Thanks for your help in advance.
KS