1. Field of the Invention
The present invention relates generally to fluid pumps and turbines, and particularly to a combined pump and energy recovery turbine that may be used, e.g., in a desalination plant for pumping seawater through a reverse osmosis membrane.
2. Description of the Related Art
Large seawater reverse osmosis (SWRO) systems are prevalent in areas that do not have natural fresh water sources, such as streams and lakes. While the efficiency of an SWRO exceeds many other desalination methods, a substantial amount of energy is still required in SWRO plant operations. The reverse osmosis chamber needs to have a supply pump feeding its chamber for continuous output of permeate (fresh water). Booster pumps are often connected to some sort of work exchanger that captures fluid pressure from high-pressure brine output of the SWRO promise to increase efficiency of the system and lower the cost of operations. A more efficient work exchanger would be desirable.
Thus, a combined pump and energy recovery turbine solving the aforementioned problems is desired.
The combined pump and energy recovery turbine is a rotary sliding vane unit that can operate as a main system pump pressurizing a system destination, such as an RO (reverse osmosis) chamber, the pumping unit incorporating an energy recovery expander for reducing the operating cost by recovering energy from a second flow that may be an unwanted byproduct from the process, for example, brine discharged at high pressure from an RO seawater desalination system. The apparatus is a hydraulic pump mechanism suitable to serve as the first input pump of an RO system. The unitary device incorporates an energy recovery expander that recovers energy from the brine output flow of the RO system. The device may include a hydrodynamic lubrication means for sliding vanes in physical contact with its pump chamber. The pump chamber walls have rotor slots that reduce frictional losses through the device and, thus, energy recovery efficiency is improved.
These and other features of the present invention will become readily apparent upon further review of the following specification and drawings.
Similar reference characters denote corresponding features consistently throughout the attached drawings.
The combined pump and energy recovery turbine unit 10, as shown in
Referring to
The multi-rotor, multi-chamber assembly shown in
A faceplate 12 covers the first module 13a. The faceplate 12 has connecting ports 14, 16, 18, and 20, which extend into the inlet and outlet headers 51a through 51d. A HP feed outlet port 14 is connected to the HP feed outlet header 51d. A LP feed inlet port 16 is connected to the LP feed inlet manifold passageway (header) 51c. An HP brine inlet port 18 is connected to the HP brine inlet manifold passageway (header) 51a. Lastly, an LP brine outlet port 20 is connected to the LP brine outlet manifold passageway (header) 51b.
It should be understood that as a vane 24 in the rotor assembly 47 sweeps through a respective chamber 99a or 99b, the vane 24 divides the chamber into an intake sub-chamber at the trailing side of the vane and a discharge sub-chamber at the leading side of the vane 24. Thus, the combined pump and energy recovery turbine 10 is powered in this manner. HP brine water travels through the HP brine water inlet port 18 and into the connected inlet header 51a to thereby enter into the corresponding crescent-shaped chamber 99a, which may be referred to as the turbine chamber 99a or turbine portion of the unit 10. High pressure of brine water on vane 24 in contact with the inner wall of the crescent-shaped chamber 99a, fed by brine water inlet header 51a, causes rotary action of rotor 47, the vane 24 sweeping through the sub-divided crescent-shaped volume, thereby decreasing the pressure of the HP intake fluid as it travels toward the low pressure brine water outlet header 51b. The high-pressure brine water is expanded and displaced by the sweeping sliding vane 24 through the discharge port 20 in communication with discharge header 51b at lower pressure.
Conversely, LP seawater travels through the LP seawater inlet port 16, through the connected inlet header 51c, and into the corresponding crescent-shaped chamber 99b, which may be referred to as the pump chamber 99b or pump portion of the unit 10. The rotary action of the rotor 47 causes the vane 24, which is in contact with inner wall of the crescent-shaped chamber 99b, to sweep through the sub-divided crescent-shaped volume, thereby increasing the pressure of the intake fluid as it travels toward the high pressure outlet header 51d. The high pressure seawater exits via the outlet header 51d, and then through the HP feed outlet port 14. As shown in
To help guide rotary motion of the vanes 24, machined cam tracks may be formed along the inner wall of oval shaped housing 30. The vane outer tips may then engage the oval shape cam tracks formed in the chamber inner wall. Inlet manifold passageways 51a, 51c are arranged in the crescent-shaped chamber proximal to a tapered end of the housing 30, and outlet passageways 51b, 51d are arranged proximal to an opposing end of the housing 30. Such an arrangement results in flow from inlet to outlet in a counter current direction within the housing module of the combined pump and energy recovery turbine 10.
As shown in
Optionally, the combined pump and energy recovery turbine 10 can also receive auxiliary mechanical power via power shaft 22. In the case where the supply pressure at the HP brine inlet 18 is less than the HP feed pressure at outlet port 14, the combined pump and energy recovery turbine 10 operates as a combination energy recovery turbine and booster pump mode. And in this case, an external booster pump 36 may not be needed to augment the pressure to the level of the discharge pressure of mean feed pump 38.
Referring to
Thus, in the exemplary SWRO combined pump and energy recovery turbine 10, a first chamber 99a and corresponding one of the sweeping sliding vanes 24 operate as an energy recovery-expander receiving high pressure brine from an RO vessel and disposing the spent brine to waste, thereby recovering energy used for pressurizing seawater in a second chamber 99b. The second chamber 99b and its corresponding one of sweeping sliding vanes 24 operate as a pump for pressurizing flow, such as seawater feed in the RO plant. The system 10 can be optimized for application in a seawater RO system to provide benefits including simplicity, compact machine size and low capital and operating costs. Long term reliability can be enhanced by employing hydrodynamic lubrication of the sliding vanes 24.
While a single rotor 47 produces a generally sinusoidal fluid flow through the pump portion of the unit, four rotors 47 that are coaxially coupled in such a manner that their vanes 24 are staggered or equally spaced radially produce fluid flow at a generally constant rate through the pump portion of the combined pump and energy recovery turbine unit 10.
Another embodiment of the combined pump and energy recovery turbine is a turbo-compressor where the first fluid flow is low pressure steam introduced through the first inlet port and the second fluid flow is high pressure steam introduced through the second inlet port. Here, the purpose of the device is compress the low pressure steam to a higher pressure using the pressure energy of available high pressure steam.
Another embodiment of the combined pump and energy recovery turbine is a turbocharger for power plants where the first fluid is air introduced at atmospheric pressure through the first inlet port and the second fluid flow is high pressure exhaust gases from the plant introduced through the second inlet port.
Still another embodiment of the combined pump and energy recovery turbine is a turbo-vacuum pump where the first fluid flow is low pressure gas or vapor from a low pressure chamber under vacuum introduced through the first inlet port and the second fluid flow is high pressure steam introduced through the second inlet port. Here, the purpose of the device is maintain vacuum or remove unwanted gases from a process chamber using the pressure energy of available high pressure steam.
It is to be understood that the present invention is not limited to the embodiments described above, but encompasses any and all embodiments within the scope of the following claims.
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Entry |
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Osama M. Al-Hawaj, “Sliding Vane Work Exchanger (SVWE)” Third International Desalination Workshop (IDW), Nov. 2010. |
Osama M. Al-Hawaj, “Theoretical Analysis of Sliding Vane Energy Recovery Device” (Abstract only) Desalination & Water Treatment, vol. 36 Issue 1-3, p. 354, Dec. 2011. |
Number | Date | Country | |
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20140202144 A1 | Jul 2014 | US |