System for reverse osmosis

Patent metadata

Field	Value
Publication number	US-2024100481-A1
Application number	US-202318347685-A
Country	US
Kind code	A1
Filing date	Jul 6, 2023
Priority date	Sep 23, 2022
Publication date	Mar 28, 2024
Grant date	—

Abstract

A system for reverse osmosis, RO, including a first RO stage (10) with a first feed inlet (11), a first brine outlet (12), and a first permeate outlet (13); a second RO stage (20) with a second feed inlet (21), a second brine outlet (22), and a second permeate outlet (23); and a pressure exchanger, PE, (40) connected between the second brine outlet (22) and the first feed inlet (11), wherein a first pressure difference Δp1 between the first brine outlet (12) and the second feed inlet (21) corresponds to a second pressure difference Δp2 between the second brine outlet (22) and the pressure exchanger (40). The invention further discloses a method for operating such a system for reverse osmosis (100).

First claim

What is claimed is:

1 . A system for reverse osmosis, RO, comprising:
a first RO stage with a first feed inlet, a first brine outlet, and a first permeate outlet; a second RO stage with a second feed inlet, a second brine outlet, and a second permeate outlet; a pressure exchanger, PE, connected between the second brine outlet and the first feed inlet, wherein a first pressure difference Δp 1 between the first brine outlet and the second feed inlet corresponds to a second pressure difference Δp 2 between the second brine outlet and the pressure exchanger.

2 . The system according to claim 1 , wherein the pressure exchanger comprises an PE HP inlet connected to the second brine outlet and an PE HP outlet connected to the first feed inlet, wherein the second pressure difference Δp 2 is occurring between the second brine outlet and the PE HP inlet.

3 . The system according to claim 1 , wherein the first pressure difference Δp 1 is utilized to create the second pressure difference Δp 2 or wherein the second pressure difference Δp 2 is utilized to create the first pressure difference Δp 1 .

4 . The system according to claim 1 , wherein the pressure exchanger is an isobaric pressure exchanger.

5 . The system according to claim 1 , wherein the pressure exchanger is a rotary pressure exchanger.

6 . The system according to claim 1 , wherein a hydraulic motor is connected between the second brine outlet and the PE HP inlet and wherein the pressure drop occurring at the hydraulic motor is the second pressure difference Δp 2 that is corresponding to the first pressure difference Δp 1 .

7 . The system according to claim 6 , wherein a pressure at the first brine outlet is smaller than a pressure at the second feed inlet and/or a hydraulic pump is interconnected between the first brine outlet and the second feed inlet.

8 . The system according to claim 1 , wherein a hydraulic pump is connected between the second brine outlet and the PE HP inlet and wherein the pressure rise occurring at the hydraulic pump is the second pressure difference Δp 2 that is corresponding to the first pressure difference Δp 1 .

9 . The system according to claim 8 , wherein a pressure at the first brine outlet is larger than a pressure at the second feed inlet and/or wherein a hydraulic motor is interconnected between the first brine outlet and the second feed inlet.

10 . The system according to claim 1 , wherein the first pressure difference Δp 1 is larger than 10 bar, preferably larger than 20 bar, and further preferably larger than 50 bar.

11 . The system according to claim 1 , wherein the first pressure difference Δp 1 is about 80% to 120% of the second pressure difference Δp 2 , preferably the first pressure difference Δp 1 is about 90% to 110% of the second pressure difference Δp 2 , and particularly preferred the first pressure difference Δp 1 is about 95% to 105% of the second pressure difference Δp 2 .

12 . The system according to claim 7 , wherein the hydraulic motor and the hydraulic pump are mechanically connected to each other, preferably via an induction motor.

13 . The system according to claim 1 , further comprising a third RO stage interconnected between the first RO stage and the second RO stage and having a third feed inlet, a third brine outlet, and a third permeate outlet, wherein the first pressure difference Δp 1 comprises a pressure difference Δp 3,1 between the first brine outlet and the third feed inlet and a pressure difference Δp 3,2 between the third brine outlet and the second feed inlet.

14 . A method of operating a system for reverse osmosis, RO, comprising a first RO stage with a first feed inlet, a first brine outlet, and a first permeate outlet, a second RO stage with a second feed inlet, a second brine outlet, and a second permeate outlet, and a pressure exchanger connected between the second brine outlet and the first feed inlet, the method comprising the steps of:
changing a pressure between the first brine outlet and the second feed inlet by a first pressure difference Δp 1 ; changing a pressure between the second brine outlet and the pressure exchanger by a second pressure difference Δp 2 corresponding to the first pressure difference Δp 1 ; and transferring hydraulic energy from a second brine flow effluent from the second brine outlet to a first feed flow provided to the first feed inlet via the pressure exchanger.

15 . The method of claim 14 for operating a system further comprising a third RO stage interconnected between the first RO stage and the second RO stage and having a third feed inlet, a third brine outlet, and a third permeate outlet, the method further comprising the steps of:
changing a pressure between the first brine outlet and the third feed inlet by a pressure difference Δp 3,1 ;
changing a pressure between the third brine outlet and the second feed inlet by a pressure difference Δp 3,2 ;
wherein the sum of pressure difference Δp 3,1 and pressure difference Δp 3,2 amounts to at least the first pressure difference Δp 1 , and
wherein at least one of the pressure difference Δp 3,1 and pressure difference Δp 3,2 is affected via one of a of a hydraulic motor and a hydraulic pump, and the pressure difference Δp 2 is affected by the other one of a hydraulic motor and a hydraulic pump.

Assignees

• Danfoss As

Inventors

• Andersen Stig Kildegaard
• Hansen Poul Erik
• Enevoldsen Georg Herborg

Classifications

• B01D2317/06

  Use of membrane modules of the same kind · CPC title

• B01D2311/14

  Pressure control · CPC title

• F04F13/00

  Pressure exchangers · CPC title

• B01D61/06 Primary

  Energy recovery · CPC title

• B01D61/026

  comprising multiple reverse osmosis steps · CPC title