Integrated reverse osmosis module with energy recovery for desalination

Patent metadata

Field	Value
Publication number	US-10953368-B2
Application number	US-201615547035-A
Country	US
Kind code	B2
Filing date	Jan 27, 2016
Priority date	Jan 27, 2015
Publication date	Mar 23, 2021
Grant date	Mar 23, 2021

Abstract

A system includes a first fluid inlet and a single reverse osmosis membrane module having a permeate outlet and a first inlet/outlet channel and a second fluid inlet/outlet channel in fluid communication with the first fluid inlet. An energy transfer system has a second fluid inlet, a brine outlet, a first energy exchanging module and a second energy exchanging module. The first and second energy exchanging modules are adapted to reversibly operate in opposite flow phases where a flow direction for the expulsion flow phase in each energy exchanging module is constant and where a flow direction for the energy recover flow phase in each energy exchanging module is constant. The single reverse osmosis membrane module is adapted to reversibly receive a feed flow through one of the first and second fluid inlet/outlet channels and produce a brine outflow through the other of the first and second inlet/outlet channels.

First claim

The invention claimed is:

1. A system comprising:
a first fluid inlet;
a single reverse osmosis membrane module having a permeate outlet and a first fluid inlet/outlet channel and a second fluid inlet/outlet channel in fluid communication with the first fluid inlet; and
an energy transfer system having an energy transfer system fluid inlet, a brine outlet, a first energy exchanging module and a second energy exchanging module, the first and second energy exchanging modules each in fluid communication with the energy transfer system fluid inlet and the brine outlet in an expulsion flow phase and in fluid communication with the first and second fluid inlet/outlet channels of the single reverse osmosis membrane module in an energy recovery flow phase;
wherein the single reverse osmosis membrane module is arranged so that it is at least partially encapsulated by the first and second energy exchanging modules;
wherein the first and second energy exchanging modules are adapted to reversibly operate in opposite flow phases where a flow direction for the expulsion flow phase in each energy exchanging module is constant and where a flow direction for the energy recover flow phase in each energy exchanging module is constant; and
wherein the single reverse osmosis membrane module is adapted to reversibly receive a feed flow through one of the first and second fluid inlet/outlet channels and produce a brine outflow through the other of the first and second inlet/outlet channels, as well as continuously producing a permeate flow that exits through the permeate outlet.

2. The system of claim 1 , wherein the system is configured to operate at a volume of less than or equal to 200 m 3 permeate per day.

3. The system of claim 1 , wherein the energy transfer system comprises a pressure exchanger and wherein the first energy exchanging module comprises a first pressure exchanging chamber comprising a first piston and the second energy exchanging module comprises a second pressure exchanging chamber comprising a second piston.

4. The system of claim 1 , further comprising a booster pump in fluid communication with the first and second energy exchanging modules when the first and second energy exchanging modules are in the energy recovery flow phase.

5. The system of claim 4 , wherein the energy transfer system comprises a pressure exchanger and wherein the first energy exchanging module comprises a first pressure exchanging chamber comprising a first piston and the second energy exchanging module comprises a second pressure exchanging chamber comprising a second piston.

6. The system of claim 5 , wherein the first and second pressure exchanging chambers each further comprise first and second channels, wherein:
when operated in a first direction, the first channel of the first pressure exchanging chamber is adapted to receive the brine outflow from the second inlet/outlet channel of the single reverse osmosis membrane module and the second channel of the first pressure exchanging chamber is adapted to provide a high pressure feed fluid to the booster pump and then to the first inlet/outlet channel of the single reverse osmosis membrane module, and the first channel of the second pressure exchanging chamber is adapted to receive feed water from the energy transfer system fluid inlet and the second channel of the second pressure exchanging chamber is adapted to expel a brine to the brine outlet of the energy transfer system; and
when operated in a second direction, the second channel of the second pressure exchanging chamber is adapted to receive the brine outflow from the first inlet/outlet channel of the single reverse osmosis membrane module and the first channel of the second pressure exchanging chamber is adapted to provide a high pressure feed fluid to the booster pump and then to the second inlet/outlet channel of the single reverse osmosis membrane module, and the second channel of the first pressure exchanging chamber is adapted to receive feed water from the fluid inlet of the energy transfer system and the first channel of the first pressure exchanging chamber is adapted to expel a brine to the brine outlet of the energy transfer system.

7. The system of claim 1 , wherein the system comprises a high pressure pump in fluid communication with the first fluid inlet and in fluid communication with one of the first and second inlet/outlet channels of the single reverse osmosis membrane module in a first flow direction and in fluid communication with the other of the first and second inlet/outlet channels of the single reverse osmosis membrane module in a second flow direction.

8. The system of claim 1 , further comprising a plurality of check valves configured to control flow of fluids through the system.

9. The system of claim 8 , wherein the check valves are controlled by actuators that are controlled by a control system.

10. The system of claim 1 , wherein the single reverse osmosis membrane module is cylindrical and the first and second energy exchanging modules together form a hollow cylinder that at least partially encapsulates the single reverse osmosis membrane module.

11. The system of claim 1 , wherein the single reverse osmosis membrane module is cylindrical and the first energy exchanging module is in the form of a concentric cylindrical channel that at least partially encapsulates the single reverse osmosis membrane module and the second energy exchanging module is in the form of a concentric cylindrical channel that at least partially encapsulates the first energy exchanging module.

12. The system of claim 1 , wherein the single reverse osmosis membrane module is cylindrical and the second energy exchanging module is in the form of a concentric cylindrical channel that at least partially encapsulates the single reverse osmosis membrane module and the first energy exchanging module is in the form of a concentric cylindrical channel that at least partially encapsulates the second energy exchanging module.

13. The system of claim 1 , wherein the single reverse osmosis membrane module is separate from the first and second energy exchanging modules.

14. The system of claim 13 , wherein the first and second energy exchanging modules are both cylindrical channels.

15. A method of producing desalinated water using the system of claim 1 , the method comprising:
providing a salinated water feed to the first fluid inlet;
reversibly operating the first and second energy exchanging modules in opposite flow phases, wherein a flow direction for the expulsion flow phase in each energy exchanging module is constant and wherein a flow direction for the energy recover flow phase in each energy exchanging module is constant;
reversibly receiving, at the single reverse osmosis membrane module, a feed flow through one of the first and second fluid inlet/outlet channels;
producing a brine outflow through the other of the first and second inlet/outlet channels; and
continuously producing a permeate flow that exits through the permeate outlet.

16. The method of claim 15 , wherein the energy transfer system further comprises a pressure exchanger and wherein the first energy exchanging module comprises a first pressure exchanging chamber comprising a first piston and the second energy exchanging module comprises a second pressure exchanging chamber comprising a second piston;
wherein the system further comprises a booster pump in fluid communication with the first and second energy exchanging modules when the first and second energy exchanging modules are in the energy recovery flow phase;
wherein, when operated in a firs

Assignees

• Univ Nanyang Tech

Inventors

• Song Jie
• Law Wing Keung

Classifications

• B01D61/08

  Apparatus therefor · CPC title

• B01D65/08

  Prevention of membrane fouling or of concentration polarisation · CPC title

• B01D2321/2083

  By reversing the flow · CPC title

• C02F1/441

  by reverse osmosis · CPC title

• Y02W10/30

  Wastewater or sewage treatment systems using renewable energies · CPC title