sujins
Industrial
- Jun 30, 2005
- 31
1)When we have the system of transfer liquid with using centrifugal pump which suction line connected from storage tanks and liquid is discharged to the process column, since the required flow rate is less than the point that performance curve meet the system curve.(Pump will operate at that point?) Then,during pump operation, we will use 2 control valves with one is the existing to control flow rate at the discharge line to column and the other one is the new pressure control valve which installed at the recycle line for the excess of flow rate to the storage tank. Since, we will not trim the impeller and will also not consider to use the variable speed drive to reduce the speed of motor. Is this concept of design able to control to achieve the desired flow rate and keep constant discharge pressure of pump. It seems like we have two control valves; one is for flow control and one for pressure control. If it's ok. Then, please suggest how to calculate to obtain the data to size the 2 mentioned control valves to get the desired flow and pressure. I mean pressure drop, flow rate of each control valve. Please help.
2) If the existing flow control valve is normally flow over from column to storage tank, but we will transfer liquid according to the above description back from storage tank to column which the flow of control valve will be flow under? Can we control that control valve with the reverse direction? Any other things that I might be forget and have to consider, please expert suggest me with the right solution.
2) If the existing flow control valve is normally flow over from column to storage tank, but we will transfer liquid according to the above description back from storage tank to column which the flow of control valve will be flow under? Can we control that control valve with the reverse direction? Any other things that I might be forget and have to consider, please expert suggest me with the right solution.