Method for converting osmotic energy into hydraulic energy and for desalination

Patent metadata

Field	Value
Publication number	US-2024252985-A1
Application number	US-202218567115-A
Country	US
Kind code	A1
Filing date	Jun 2, 2022
Priority date	Jun 8, 2021
Publication date	Aug 1, 2024
Grant date	—

Abstract

The method p1 for converting osmotic energy into hydraulic energy and the method p2 for desalination, include pressurisation/depressurisation and isochoric washing of an aqueous solution containing a salt in the presence of a selective hydrophobic nanoporous material of which the nanoporous volume within the material is only accessible to fresh water and which has a nanoporosity volume fraction ranging from 0.2 to 1 so as to convert osmotic energy into hydraulic energy or conversely to desalinate water, preferably sea water or brine.

First claim

1 . A process for converting osmotic energy into hydraulic energy, comprising:
1a) contacting (i) a first aqueous solution comprising a salt, and (ii) a selective hydrophobic nanoporous material whose nanopore volume within the material is accessible only to fresh water and which has a volume fraction of nanoporosity in a range of from 0.2 to 1, to obtain a mixture, 1b) pressurizing the mixture to a pressure in a range of from 10 to 1000 bar, to obtain a pressurized mixture wherein water intrudes into the nanoporous material, to obtain a pressurized mixture, 1c) carrying out a first_isochoric washing of the pressurized mixture using a second aqueous solution comprising a salt, to obtained a washed mixture, and 1d) depressurizing the washed mixture, wherein water is expulsed from the nanoporous material, diluting the aqueous solution, and collecting hydraulic energy, wherein a salt concentration of the aqueous solution is greater than a salt concentration of the first aqueous solution, a difference in salt concentration between the first aqueous solution and the second aqueous solution being within a range of from 0.5 to 25 mol/L.

2 . The process as claimed in claim 1 , wherein the second aqueous solution has a salt concentration of less than or equal to 25 mol/L.

3 . The process as claimed in claim 1 , wherein the first aqueous solution has a salt concentration in a range of from 0 to 2 mol/L.

4 . The process as claimed in claim 1 , wherein the nanoporous material is selected from the group consisting of MOFs, zeolites, imogolites, mesoporous silicas, mesoporous organosilicon compounds and aerogels.

5 . The process as claimed in claim 1 , wherein the nanoporous material has pores whose mean diameter is in a range of from 0.5 to 5 nm.

6 . The process as claimed in claim 1 , wherein the nanoporous material has constrictions whose mean diameter is in a range of from 0.2 to 1 nm.

7 . The process as claimed in claim 1 , wherein a volume of nanoporous material relative to a volume of the reaction medium represents a ratio M (v/v) in a range of 0.2 to 1.

8 . The process as claimed in claim 1 , further comprising 1e) carrying out a second isochoric washing of the mixture obtained at the end of the depressurizing, diluting, and collecting 1d) using a first aqueous solution.

9 . The process as claimed in claim 1 , further comprising converting the hydraulic energy collected in the collecting 1 d) into mechanical or electrical energy.

10 . The process as claimed in claim 8 , wherein the pressurizing 1b), the first isochoric washing 1c), the depressurizing, diluting, and collecting 1d), and the second isochoric washing 1e) are repeated a number n of iterations, n being an integer greater than or equal to 2.

11 . The process as claimed in claim 1 , which is performed at a temperature in a range of from 5 to 150° C.

12 . A process for desalinating a solution comprising a salt, comprising:
2a) contacting (i) a first aqueous solution comprising a salt, and (ii) a selective hydrophobic nanoporous material whose nanopore volume within the material is accessible only to fresh water and which has a volume fraction of nanoporosity in a range of from 0.2 to 1, to obtain a mixture, 2b) pressurizing the mixture to a pressure in a range of from 10 to 1200 bar, wherein water intrudes into the nanoporous material, to obtain a pressurized mixture, 2c) carrying out a first isochoric washing of the pressurized mixture using a third aqueous solution, the third aqueous solution being pure water or fresh water, to obtain a washed mixture, and 2d) depressurizing the washed mixture, wherein water is expulsed from the nanoporous material, diluting the third aqueous solution, and collecting salt-depleted water.

13 . The process as claimed in claim 12 , further comprising 2c) carrying out a second isochoric washing of the washed mixture obtained at the end of the depressurizing, diluting, and collecting 2 d), the second isochoric washing being carried out using a second aqueous solution.

14 . The process as claimed in claim 13 , wherein the pressurizing 2 b), the first isochoric washing 2 c), the depressurizing, diluting and collecting 2d) and the second isochoric washing 2 c) are repeated a number m of iterations, m being an integer greater than or equal to 2.

15 . The process as claimed in claim 12 , wherein, in the contacting 2a), the volume fraction of nanoporosity of the selective hydrophobic nanoporous material has a in a range of from 0.3 to 0.6.

16 . The process as claimed in claim 12 , wherein, in the pressurizing 2b), the mixture is pressurized to a pressure in a range of from 200 to 800 bar.

17 . The process as claimed in claim 1 , wherein, in the contacting 1a), the volume fraction of nanoporosity of the selective hydrophobic nanoporous material has a in a range of from 0.3 to 0.6.

18 . The process as claimed in claim 1 , wherein, in the pressurizing 1b), the mixture is pressurized to a pressure in a range of from 10 to 500 bar.

19 . The process as claimed in claim 1 , wherein, in the first isochoric washing 1c), the second aqueous solution comprises the salt selected from alkali metal and/or alkaline earth metal salts.

20 . The process as claimed in claim 1 , wherein the nanoporous material is selected from the group consisting of ZIF-8, Cu2(tebpz), silicalite, chabazite and SSZ-24.

Assignees

• Univ Grenoble Alpes
• Centre Nat Rech Scient

Inventors

• Picard Cyril
• Charlaix Elisabeth
• Chèvremont William

Classifications

• C02F2303/10

  Energy recovery · CPC title

• C02F2103/08

  Seawater, e.g. for desalination · CPC title

• C02F1/445

  by forward osmosis · CPC title

• B01D2325/38

  Hydrophobic membranes · CPC title

• B01D2325/027

  Nonporous membranes · CPC title