Method of preventing damage to a pump
A method for preventing damage to a multiphase pump includes measuring a differential pressure of a fluid across the pump and an axial position of a rotor of the pump over a time period, calculating a pressure fluctuation by measuring a difference between a maximum and a minimum value of the measured differential pressure over the time period, calculating a dynamic axial position by measuring a difference between a maximum and a minimum value of the measured axial position of the rotor over the time period, comparing the calculated pressure fluctuation with an expected pressure fluctuation value, comparing the calculated dynamic axial position with an expected dynamic axial position value, and selecting an operating condition of the pump based on the comparison of the calculated pressure fluctuation with the expected pressure fluctuation value and of the calculated dynamic axial position with the expected dynamic axial position value.
1. A method for preventing damage to a multiphase pump, the method comprising:
measuring a differential pressure of a fluid across the multiphase pump over a time period;
measuring an axial position of a rotor of the multiphase pump over the time period;
calculating a pressure fluctuation by measuring a difference between a maximum value of the differential pressure which was measured and a minimum value of the differential pressure which was measured over the time period;
calculating a dynamic axial position by measuring a difference between a maximum value of the axial position of the rotor which was measured and a minimum value of the axial position of the rotor which was measured over the time period;
comparing the pressure fluctuation of the multiphase pump which was calculated with an expected pressure fluctuation value;
comparing the dynamic axial position of the rotor which was calculated with an expected dynamic axial position value; and
selecting an operating condition of the multiphase pump from one of an expected operating condition, a surge operating condition, and a choke operating condition based on the comparison of the pressure fluctuation of the multiphase pump which was calculated with the expected pressure fluctuation value, and based on the comparison of the dynamic axial position of the rotor which was calculated with the expected dynamic axial position value.
2. The method as recited in claim 1 , wherein the expected pressure fluctuation value is a range of pressure fluctuation values.
3. The method as recited in claim 1 , wherein the expected dynamic axial position value of the rotor is a range of axial position values.
4. The method as recited in claim 1 , wherein the measuring of the differential pressure of the fluid across the multiphase pump over the time period is performed by measuring a pressure of the fluid at an inlet of the multiphase pump and at an outlet of the multiphase pump over the time period.
5. The method as recited in claim 1 , wherein both the differential pressure of the fluid across the multiphase pump and the axial position of the rotor of the multiphase pump over the time period are measured.
6. The method as recited in claim 1 , further comprising:
identifying the surge operating condition as existing when the pressure fluctuation is not equal to at least one of the expected pressure fluctuation value and the expected dynamic axial position value.
7. The method as recited in claim 6 , further comprising:
increasing a fluid flow to the multiphase pump to reduce a fluid pressure at an outlet of the multiphase pump to change the operating condition of the multiphase pump from the surge operating condition to a normal operating condition when the pressure fluctuation is equal to the expected pressure fluctuation value.
8. The method as recited in claim 7 , further comprising increasing the fluid flow through the multiphase pump and thereby reducing the fluid pressure at the outlet of the multiphase pump by:
increasing a pump operating speed.
9. The method as recited in claim 7 , further comprising increasing the fluid flow through the multiphase pump and thereby reducing the fluid pressure at the outlet of the multiphase pump by:
connecting an inlet of the multiphase pump to a fluid source via a source conduit;
connecting an outlet of the multiphase pump to a fluid sink via a sink conduit; and
opening a recirculation valve in the sink conduit to flow fluid back to the fluid source via a recirculation conduit.
10. The method as recited in claim 6 , further comprising:
identifying the choke operating condition as existing when the dynamic axial position is not equal to the expected dynamic axial position value.
11. The method as recited in claim 10 , further comprising:
increasing a fluid pressure at an outlet of the multiphase pump to change the operating condition of the multiphase pump from the choke operating condition to a normal operating condition when the dynamic axial position is equal to the expected dynamic axial position value.
12. The method as recited in claim 11 , further comprising:
connecting an inlet of the multiphase pump to a fluid source via a source conduit;
connecting an outlet of the multiphase pump to a fluid sink via a sink conduit, and at least partially closing a discharge valve in the sink conduit so as to increase a fluid pressure at the outlet of the multiphase pump.
13. The method as recited in claim 1 , further comprising:
measuring a vibration of the multiphase pump; and
comparing the vibration measured to an expected vibration measurement.
14. The method as recited in claim 1 , wherein the multiphase pump is a subsea pump.
15. The method as recited in claim 1 , further comprising:
providing an alert to a user when at least one of:
the pressure fluctuation is not equal to the expected pressure fluctuation value, and
the dynamic axial position is not equal to the expected dynamic axial position value.
16. A piping installation comprising:
a multiphase pump comprising a pump inlet, a pump outlet and a rotor;
a device for measuring a differential pressure between the pump inlet and the pump outlet; and
a device for measuring an axial position of the rotor,
wherein,
the piping installation is configured to prevent damage to the multiphase pump based on the method as recited in claim 1 .
17. The piping installation as recited in claim 16 , wherein the device for measuring the differential pressure between the pump inlet and the pump outlet comprises:
a pressure transmitter which is arranged at the pump inlet to measure a pressure at the pump inlet; and
a pressure transmitter which is arranged at the pump outlet to measure a pressure at the pump outlet,
so as to calculate the differential pressure therebetween.
18. The piping installation as recited in claim 16 , wherein the device for measuring the axial position of the rotor of the multiphase pump comprises proximity sensors which are coupled to the multiphase pump.
19. The piping installation as recited in claim 16 , wherein the device for measuring the axial position of the rotor of the multiphase pump comprises at least one accelerometer which is coupled to the multiphase pump, the at least one accelerometer being configured to measure a vibrational movement of the multiphase pump and to compare the vibrational movement with an expected vibrational movement value.