Methods and systems for cooling a pressurized fluid with a reduced-pressure fluid
Systems and methods for reducing the pressure of a first pressurized fluid, thereby reducing the temperature of the pressurized fluid, and utilization of the reduced-pressure and temperature fluid to cool a second fluid. Such an approach can enable a reduction in the size and weight of a hydraulic system, utilize waste energy in a system, and/or minimize electrical power requirements of a system, among other benefits.
1. A pumping system, comprising:
a turbo-pump that includes:
a housing;
a pump located in the housing and configured to pressurize a hydraulic fluid in a hydraulic circuit; and
an expander located in the housing and mechanically coupled to the pump, the expander configured to be coupled to a pressurized gas source located exteriorly of the housing for driving the pump;
the pumping system further comprising:
a heat exchanger coupled to an outlet of the expander and configured to be coupled to the hydraulic circuit for cooling the hydraulic fluid with the pressurized gas discharged from the expander; and
a valve disposed upstream of an inlet of the expander and configured to control the flow of the pressurized gas into the expander according to at least one of a pressure of the hydraulic fluid, a temperature of the hydraulic fluid, or a speed of the pump.
2. The pumping system of claim 1 , wherein the pump and the expander are coupled by a shaft, the pumping system further including a hydrodynamic fluid bearing coupled to the shaft, wherein the bearing utilizes the hydraulic fluid from the hydraulic circuit as a bearing working fluid.
3. The pumping system of claim 2 , wherein the pump is a centrifugal pump and the expander is an axial turbine.
4. The pumping system of claim 1 , further comprising a bypass valve coupled to the hydraulic circuit and located upstream of the heat exchanger, wherein the bypass valve is configured to open when a temperature of the hydraulic fluid drops below a threshold value to thereby cause at least a portion of the hydraulic fluid to bypass the heat exchanger.
5. The pumping system of claim 1 , wherein the hydraulic fluid is water, mineral oil, rapeseed oil, canola oil, glycol, ester oil, organophosphate oil, polyalphaolefin, propylene glycol, or a silicone oil.
6. The pumping system of claim 1 , wherein the pressurized gas is air, hydrogen, natural gas, methane, nitrogen, or carbon dioxide.
7. The pumping system of claim 1 , wherein the valve is configured to adjust a position of the valve to maintain the pressure of the hydraulic fluid at a substantially constant pressure, wherein the pressure is between 1,000 psi and 3,500 psi.
8. The pumping system of claim 1 , wherein the expander is configured to be in an open loop system wherein the pressurized gas discharged from the expander does not return to the inlet of the expander.
9. A controller for a pumping system, the pumping system including:
a pump configured to pressurize a hydraulic fluid in a hydraulic circuit;
an expander mechanically coupled to the pump, the expander configured to be coupled to a pressurized gas source for powering the expander and the pump;
a heat exchanger coupled to an outlet of the expander and configured to be coupled to the hydraulic circuit for cooling the hydraulic fluid with the pressurized gas discharged from the expander;
a control valve disposed upstream of an inlet of the expander and configured to control the flow of the pressurized gas into the expander; and
a bypass valve coupled to the hydraulic circuit and located upstream of the heat exchanger for bypassing the heat exchanger;
wherein the controller is configured to perform operations comprising:
receiving a pressure value corresponding to a pressure of the hydraulic circuit;
controlling a position of the control valve according to the pressure value to maintain a substantially-constant pressure in the hydraulic circuit; and
opening the bypass valve in response to determining a temperature of the hydraulic fluid is below a threshold value to thereby cause at least a portion of the hydraulic fluid to bypass the heat exchanger.
10. The controller of claim 9 , wherein the expander is coupled to the pump by a shaft, wherein the controller is further configured to receive a shaft speed value corresponding to a speed of the shaft, and wherein the step of controlling a position of the control valve includes controlling the position of the control valve according to the pressure value and the shaft speed value.
11. The controller of claim 9 , wherein controller is further configured to receive a temperature value corresponding to the temperature of the hydraulic fluid, and wherein the step of controlling a position of the control valve includes controlling the position of the control valve according to the pressure value and the temperature value.
12. The controller of claim 9 , wherein the expander is configured to be in an open loop system wherein the pressurized gas discharged from the expander does not return to the inlet of the expander.
13. A method of controlling a pressure of a hydraulic circuit with a pumping system, the pumping system including: a pump configured to pressurize a hydraulic fluid in the hydraulic circuit; an expander mechanically coupled to the pump, the expander configured to be coupled to a pressurized gas source for driving the pump; a heat exchanger coupled to an outlet of the expander and configured to be coupled to the hydraulic circuit for cooling the hydraulic fluid with the pressurized gas discharged from the expander; and a valve disposed at an inlet of the expander and configured to control the flow of the pressurized gas into the expander; the method comprising: receiving at least one of a pressure of the hydraulic fluid, a temperature of the hydraulic fluid, or a speed of the pump; adjusting a position of the valve according to the received pressure, temperature, or speed to thereby control a power output of the expander and pump to maintain the pressure of the hydraulic fluid at a substantially constant value; wherein the pumping system further comprises a bypass valve coupled to the hydraulic circuit and located upstream of the heat exchanger, the method further comprising opening the bypass valve in response to the temperature of the hydraulic fluid dropping below a threshold value to thereby cause at least a portion of the hydraulic fluid to bypass the heat exchanger.
14. The method of claim 13 , wherein the hydraulic fluid is water, mineral oil, rapeseed oil, canola oil, glycol, ester oil, organophosphate oil, polyalphaolefin, propylene glycol, or a silicone oil.
15. The method of claim 13 , wherein the pressurized gas is air, hydrogen, natural gas, methane, or carbon dioxide.
16. The method of claim 13 , wherein the substantially constant value is between 1,000 psi and 3,500 psi.
17. The method of claim 13 , wherein the expander is configured to be in an open loop system wherein the pressurized gas discharged from the expander does not return to the inlet of the expander.