Centrifugal pump for de-watering
A method of de-watering during intermittent dry running periods with a self-priming centrifugal pump is presented. Centrifugal pumps, as opposed to diaphragm pumps, are advantageous because they are less expensive and can provide greater capacity. The shaft seals are sensitive, however, to frictional heating when water flow is interrupted. In some situations, this fractional heating may desiccate self-priming. The inventive concept provides a continuous stream of pressurized water moving through the pump to cool the seal and sustain priming capability without substantially impairing the ability of the pump to resume wet operation.
1. A method comprising:
providing a self-priming centrifugal pump comprising:
an inlet port;
an impeller within a volute;
an internal chamber in fluid communication with the volute to deliver water from an air-water mixture expelled by the impeller back to the volute during a recycling mode; and
a discharge port to discharge air from the air-water mixture out of the self-priming centrifugal pump during the recycling mode; and
injecting water into the self-priming centrifugal pump to maintain a reservoir of water within the volute sufficient to cool a shaft seal of the self-priming centrifugal pump and generate the air-water mixture at the impeller to provide suction at the inlet port, wherein injecting the water into the self-priming centrifugal pump comprises injecting the water into the self-priming pump through the discharge port at a fraction of a pumping capacity of the self-priming centrifugal pump.
2. The method of claim 1 , wherein the water is under line pressure.
3. The method of claim 1 , wherein injecting the water at the fraction of the pumping capacity comprises injecting the water at a rate of approximately 3-5 gallons per minute to the self-priming centrifugal pump which is capable of operating at a rate of approximately 100-150 gallons per minute in a suction mode.
4. A method comprising:
providing a self-priming centrifugal pump comprising:
an inlet port;
an impeller within a volute;
an internal chamber in liquid communication with the volute to deliver liquid from a gas-liquid mixture expelled by the impeller back to the impeller within the volute during a recycling mode; and
a discharge port to discharge gas from the gas-liquid mixture out of the self-priming centrifugal pump during the recycling mode; and
providing a coupling in fluid communication with the volute, the coupling sized sufficient to accommodate delivery of a pressurized liquid from a pressurized liquid source to the volute in a quantity sufficient to support generation of the gas-liquid mixture to provide suction at the inlet port, wherein the coupling is in fluid communication with the volute through one of:
the discharge port of the self-priming centrifugal pump;
the inlet port of the self-priming centrifugal pump; and
a drain port of the self-priming centrifugal pump.
5. The method of claim 4 , wherein the pressurized liquid is water under line pressure.
6. The method of claim 4 , wherein the quantity sufficient to support generation of the gas-liquid mixture to provide suction at the inlet port is less than a pumping capacity of the self-priming centrifugal pump.
7. A system comprising:
a self-priming centrifugal pump comprising:
an impeller;
a volute at least partially surrounding the impeller, wherein the volute is sized to be partially filled with a liquid and partially filled with a gas during a recycle mode, the liquid and gas forming a mixture in response to rotation of the impeller during the recycle mode; and
an internal chamber disposed on a side of the volute opposite the impeller, the internal chamber having a geometry to direct liquid separated from the mixture toward the impeller during the recycle mode; and
a coupler attached to the self-priming centrifugal pump, the coupler forming a liquid path to provide a pressurized liquid from a pressurized liquid source to the volute in a quantity sufficient to support generation of suction at an inlet port, wherein liquid from the inlet port flows to the volute during a suction mode, wherein the coupler is attached to the self-priming centrifugal pump one of:
upstream of an inlet port of the self-priming centrifugal pump;
at approximately a discharge port of the self-priming centrifugal pump, and in direct fluid communication with a discharge pathway of fluid from the self-priming centrifugal pump; and
at approximately a drain port of the self-priming centrifugal pump.
8. The system of claim 7 , wherein the geometry of the internal chamber is further to direct liquid away from the impeller during the suction mode.
9. The system of claim 7 , wherein the coupler further comprises a backpressure regulator to substantially prevent flow through the coupler away from the self-priming centrifugal pump.
10. The system of claim 7 , wherein the quantity to support the generation of suction at an inlet port is less than a pumping capacity of the self-priming centrifugal pump.
11. The system of claim 7 , wherein the pressurized liquid is delivered to the self-priming centrifugal pump at approximately 3-10 gallons per minute and the self-priming centrifugal pump pumps at approximately 100-150 gallons per minute in the suction mode.