IP Library Granted Patent US 12,258,286
Granted Patent B2
US 12,258,286 · App. 17/617,387 · Granted Mar 25, 2025

Method of concentrating high-salinity raw water

Inventors: Jongbum Park (Daejeon, KR); Phill Lee (Daejeon, KR); Younghoon Ko (Daejeon, KR); Young Jun Shin (Daejeon, KR)
Assignee: LG Chem, Ltd.
C02F1/441B01D61/025
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Quick Facts
Patent No.
US 12,258,286
App. No.
17/617,387
Granted
Mar 25, 2025
Kind
B2
Abstract

Provided is a method for concentrating high-salinity raw water to obtain produced water satisfying Equation 1: N s =B *( C m −C p )  <Equation 1> wherein: B is a salt permeability constant (B-value), and is 3 GFD≤B≤150 GFD, N s is an amount of salt permeating the separation membrane (GFD*ppm), and has a value of F p *C p , C m is a raw water-side separation membrane surface concentration (membrane concentration) (ppm), C p is a produced water salt concentration (permeate concentration) (ppm), and F p is produced water flux (permeate flux), and is 5 GFD≤F p ≤100 GFD, by the method comprising passing raw water having a salt concentration of 70,000 ppm or greater through a separation membrane at a temperature of 40° C. or less and a pressure of 1,200 psi or less.

Claims (17)

1. A method for concentrating high-salinity raw water to obtain produced water satisfying the following <Equation 1>, the method comprising passing the high-salinity raw water having a salt concentration of 70,000 ppm or greater through a separation membrane at a temperature of 40° C. or less and a pressure of greater than or equal to 400 psi and less than or equal to 900 psi:

N s =B *( C m −C p ),  <Equation 1>

wherein in the <Equation 1>:

B is a salt permeability constant (B-value) of the separation membrane, and is 3 gallons per square foot per day (GFD) (gal/ft 2 /day)≤B≤150 gallons per square foot per day (GFD) (gal/ft 2 /day);

N s is an amount of salt permeating the separation membrane (GFD*ppm), and has a value of F p *C p ;

C m is a raw water-side separation membrane surface concentration (membrane concentration) (ppm); and

C p is a produced water salt concentration (permeate concentration) (ppm),

wherein F p is produced water flux (permeate flux), and is 5 GFD≤F p ≤100 GFD,

wherein an osmotic pressure of the produced water is from 15% to 90% of an osmotic pressure of the high-salinity raw water, and

wherein the separation membrane is a reverse osmosis membrane.

2. The method for concentrating high-salinity raw water of claim 1 , wherein the high-salinity raw water has a salt concentration of greater than or equal to 70,000 ppm and less than or equal to 200,000 ppm.

3. The method for concentrating high-salinity raw water of claim 1 , wherein the pressure is greater than or equal to 400 psi and less than or equal to 800 psi.

4. The method for concentrating high-salinity raw water of claim 1 , wherein salt rejection of the produced water satisfies the following <Equation 2>, and is greater than or equal to 10% and less than or equal to 85%:

salt rejection=(1− C p /C f )*100(%)  <Equation 2>

in the <Equation 2>:

C p is a produced water salt concentration (permeate concentration) (ppm); and

C f is a raw water salt concentration (feed concentration) (ppm).

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 24, 2025
From: LG CHEM, LTD.
To: NANOH2O CO., LTD.
Reel/Frame 073784/0326 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 8, 2021
From: PARK, JONGBUM; LEE, PHILL; KO, YOUNGHOON; SHIN, YOUNG JUN
To: LG CHEM, LTD.
Reel/Frame 058333/0310 →
Priority Claims (1)
KR 10-2019-0119618 · Sep 27, 2019 · national
Continuity (1)
Related Publication 20220250949A1 · Aug 11, 2022
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