The reverse osmosis (RO) process uses a set of membrane elements that allow solvent (e.g., water) to pass through the membrane but blocks dissolved solids (e.g., salts). RO is used for desalination of brackish water and seawater where a feed stream is separated into a freshwater stream (called permeate) by the membrane and the balance is rejected as a concentrated brine stream (called concentrate or brine) which exits the membrane at a pressure slightly lower than the feed pressure entering the membrane array. This discussion will focus on desalination however it equally applies to all separation processes with any type of solvent that use membranes.
Feed water at low pressure passes through pipe 1 to HPP 2 that raises pressure of the feed water. The pressurized feed then passes through pipe 3 to pump section 4 of turbo 34 that provides an additional pressure increase. The pressurized feed pass through pipe 5 to membrane stage 31. A fraction of the feed passes through the membrane as fresh water and exits at low pressure through pipe 22 connected to manifold 24. The remaining fluid, now a concentrated brine exits membrane 6 through pipe 7 and enters pump section 8 of turbo 33 to receive a pressure boost. The highly pressurized brine enters membrane 32. A fraction of the brine passes through the membrane as fresh water at low pressure and exits through pipe 23 that is connected to manifold 24. High-pressure brine exits membrane 32 by pipe 11 which is connected to turbine section 12 of turbo 33. A portion of the hydraulic energy from the high-pressure brine is used to energize pump section 8 of turbo 33. The partially depressurized brine passes through pipe 13 to turbine section 14 of turbo 34. The remaining hydraulic energy energizes pump section 4 of turbo 34. The depressurized brine exits turbo 34 through pipe 15 and is disposed in drain 16.
Turbo 34 contains a rotor connecting pump section 4 and turbine section 14 on a common shaft 22 that extends to motor 23 controlled by Variable Frequency Drive (VFD) 24. Motor 23 speed can increase rotor speed to generate additional pressure in pump section 4 as needed to meet process requirements. The ability of turbo 34 with attached motor 23 and VFD 24, collectively called a HEMI 35, means that pump 2 can run at a constant speed as pressure regulation is provided by HEMI 34. Thus, a VFD is not needed on pump 2. On large salt water reverse osmosis (SWRO) system, pump 2 can require an input power of over 2.0 megawatts which requires a medium voltage VFD which is very expensive, dissipates up to 4% of the electrical energy in the form of heat and can be unreliable. Thus, use of the HEMI and its relatively small and inexpensive VFD provides a significant savings in capital and operating costs.
However, membrane stages 31 and 32 require a gradual pressure rise during startup and gradual pressure reduction during shutdown to prevent damage to the membrane surfaces and spacers that support the membrane surfaces. The duration of the start and stop cycles may be over 15 minutes. A direct online (DOL) motor start takes only a few seconds to reach synchronous speed resulting in a pressure rise much too fast for optimal membrane life. Electronic soft starters and auto-transformers are suitable to ramp up and ramp down motor speeds but are suitable only for smaller motors. Only VFDs are suitable for gradual ramp up and ramp down of motor speed for very large motors used in large scale RO facilities.
Relevant prior art is illustrated in
Power bus 40, connected to the utility grid, is energized to a medium voltage (typically 4,400 to 12,000 volts). VFD 42 is connected to power bus 40 in the input side by circuit 41 and connected to VFD output bus 52 by circuit 51. One input of A/B switches 44A, 44B and 44C is connected to power bus 40 by circuits 43A, 43B and 43 C respectively. The other input of A/B switches 44A, 44B and 44C are connected to VFD output bus 52 by circuits 45A, 45B and 45C respectively.
The output circuit of A/B switches 44A, 44B and 44C are connected to circuits 46A, 46B and 46C respectively that are connected to motors 47A, 47B and 47C respectively. Motors 47A, 47B and 47C are connected to pumps 49A, 49B and 49C through shafts 48A, 48B and 48C respectively.
To illustrate the operating principles, if motor 47A needs to be gradually ramped up to synchronous speed, A/B switch 44A is set to connect circuit 46A to VFD output bus 52 by circuit 45A. VFD 42 is activated and gradually increase the frequency of power in VFD output bus 52 which cause motor 47A to gradually increase in speed. Once motor 47A reaches synchronous speed, A/B switch 44A changes input from VFD output bus 52 to power bus 40. VFD 42 may now be de-energized and is available to start or stop other motors. Thus, a single VFD can be used to gradually start and stop multiple motors one at a time. This saves considerable costs by eliminating multiple VFDs and eliminates energy losses associated with VFDs during normal operation of the motors.
However, the above system cannot be used for motors that drive high-pressure pumps in RO systems due to the need to adjust membrane pressure due to changing feed hence motor speed throughout operation of the RO system.
Utilizing a central variable frequency drive to control a reverse osmosis system with multiple membranes and energy recovery turbos.
The invention allows a single VFD to start and stop multiple RO trains that are equipped with the HEMI.
To illustrate functionality of the invention, train 100 will be brought online. VFD 42 begins to output power starting from zero (0) Hz. That power passes to VFD output bus 52 via circuit 51. Simultaneously, A/B switch 44A connects VFD output bus 52 to motor 20A which starts rotation. Under preprogramed control, the VFD 42 Hz output is increased to ramp up the speed of motor 20A until synchronous speed is achieved. At that point, A/B switch 44A disconnects VFD bus 52 and connects the train 100 to line power bus 41 by moving the switch 44A from engagement with circuit 45A to engagement with circuit 43A. Train 100 is now running on direct line power represented by power bus 41. HEMI 34A now controls flows and pressures in train 100 while HP pump 2A operates at constant (synchronous) speed.
To illustrate another function, operating train 101 is to be taken offline. VFD 42 is energized to provide power with synchronous frequency to VFD bus 52. A/B switch 44B switches from power bus 41 to VFD output bus 52. Next, VFD 42 gradually reduces frequency output, hence motor speed, until reaching zero (0). VFD 42 is de-energized and A/C switch 44B is set to disconnect position where the A/C switch 44C is not connected to power bus 41 or VFD bus 52. The three positions for the A/C switch 44A, 44B and 44C are shown in
As shown in
This application claims the benefit of provisional application Ser. No. 63/427,281, filed Nov. 22, 2022.
Number | Date | Country | |
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63427281 | Nov 2022 | US |