Subsea compressor cleaning method wherein the cleaning liquid is retrieved from the multiphase process fluid
US-9518588-B2 · Dec 13, 2016 · US
US10330122B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10330122-B2 |
| Application number | US-201514959187-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 4, 2015 |
| Priority date | Dec 18, 2014 |
| Publication date | Jun 25, 2019 |
| Grant date | Jun 25, 2019 |
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An operating method for a pump includes providing a return line for returning the fluid from a high-pressure side to a low-pressure side, controlling a control valve in the return line with a surge control unit for avoiding an unstable operating state, the control valve controlling the throughflow through the return line, storing a limit curve for a control parameter in the surge control unit, comparing an actual value of the control parameter with the limit curve during the operation of the pump; and when the actual value of the control parameter reaches the limit curve, controlling the control valve in the return line such that the actual value of the control parameter is moved away from the limit curve, an operating parameter of the pump being used as the control parameter.
Opening claim text (preview).
The invention claimed is: 1. An operating method for a pump for conveying a fluid from a low-pressure side to a high-pressure side, the method comprising: providing a return line for returning the fluid from the high-pressure side to the low-pressure side; controlling a control valve in the return line with a surge control unit for avoiding an unstable operating state, the control valve controlling throughflow through the return line; storing a limit curve for a control parameter in the surge control unit; comparing an actual value of the control parameter with the limit curve during the operation of the pump; and when the actual value of the control parameter reaches the limit curve, controlling the control valve in the return line such that the actual value of the control parameter is moved away from the limit curve, an operating parameter of the pump being used as the control parameter. 2. The method in accordance with claim 1 , further comprising indicating, with the limit curve, a unique relationship between the operating parameter and a pressure difference generated by the pump. 3. The method in accordance with claim 1 , further comprising detecting the pressure difference between the pressure at an inlet and the pressure at an outlet of the pump by measurement for comparison of the actual value of the operating parameter with the limit curve. 4. The method in accordance with claim 1 , wherein the operating parameter is in a unique relationship with a torque at which the pump is driven. 5. The method in accordance with claim 1 , wherein a torque at which the pump is driven is used as the operating parameter. 6. The method in accordance with claim 5 , further comprising indicating, with the limit curve, a dependence of the torque on the pressure difference at which the pump is still operated in a stable operating state. 7. The method in accordance with claim 1 , further comprising fixing the limit curve at a spacing from a lower surge limit line, the lower surge limit line indicating a respective value of the operating parameter at which the pump changes into an unstable operating state. 8. The method in accordance with claim 7 , further comprising determining the lower surge limit line using experimental test data by which determination the pump is led into an unstable operating state. 9. The method in accordance with claim 7 , wherein empirical values are used for determining the lower surge limit line. 10. The method in accordance with claim 1 , wherein the surge control unit is integrated into a control device programmed to control the pump. 11. The method in accordance with claim 1 , wherein the actual value of the operating parameter is provided by a variable frequency drive for the pump. 12. The method in accordance with claim 1 , wherein the pump is used as a booster pump in oil production and gas production. 13. The method in accordance with claim 1 , wherein the pump is used as a booster pump in sub-sea oil production and gas production. 14. The pump in accordance with claim 1 , wherein the pump is a multiphase pump. 15. A pump for conveying a fluid from a low-pressure side to a high-pressure side, comprising: an inlet and an outlet for the fluid; and a surge control unit configured to avoid an unstable operating state, which provides a control signal for a control valve in a return line for returning the fluid from the high-pressure side to the low-pressure side, and including a limit curve for a control parameter, the surge control unit being configured to compare an actual value of the control parameter during the operation of the pump with the limit curve and provide the control signal when the actual value of the control parameter reaches the limit curve, the control signal being capable of controlling the control valve in the return line such that the actual value of the control parameter moves away from the limit curve, the control parameter being an operating parameter of the pump. 16. The pump in accordance with claim 15 , wherein the operating parameter is a torque configured to drive the pump and the limit curve indicates a dependence of the torque on a pressure difference between a pressure at the inlet and a pressure at the outlet. 17. The pump in accordance with claim 15 , wherein the pump is a centrifugal pump. 18. The pump in accordance with claim 15 , wherein the pump is a pressure-elevating pump for oil production and gas production. 19. The pump in accordance with claim 15 , wherein the pump is a pressure-elevating pump for sub-sea oil production and gas production. 20. The pump in accordance with claim 15 , wherein the pump is a multiphase pump.
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