Production of ultra-high-density brines using transiently-operated desalination systems

Patent metadata

Field	Value
Publication number	US-11084736-B2
Application number	US-201916596975-A
Country	US
Kind code	B2
Filing date	Oct 9, 2019
Priority date	May 21, 2015
Publication date	Aug 10, 2021
Grant date	Aug 10, 2021

Abstract

Systems and methods related to desalination systems are described herein. According to some embodiments, the desalination systems are transiently operated and/or configured to facilitate transient operation. In some embodiments, a liquid stream comprising water and at least one dissolved salt is circulated through a fluidic circuit comprising a desalination system. In some embodiments, a portion of the desalination system (e.g., a humidifier) is configured to remove at least a portion of the water from the liquid stream to produce a concentrated brine stream enriched in the dissolved salt. In certain cases, the concentrated brine stream is recirculated through the fluidic circuit until the concentrated brine stream reaches a relatively high density (e.g., at least about 10 pounds per gallon) and/or a relatively high salinity (e.g., a total dissolved salt concentration of at least about 25 wt %). In certain embodiments, additional salt is added to the concentrated brine stream to produce an ultra-high-density brine stream (e.g., a brine stream having a density of at least about 11.7 pounds per gallon). Some aspects relate to a system that is configured to promote energy efficiency by recovering heat from the recirculated concentrated brine stream upon discharge from the fluidic circuit.

First claim

What is claimed is:

1. A method, comprising:
supplying a first liquid stream comprising water and a dissolved salt to a first fluidic circuit comprising a first humidifier, wherein:
the first humidifier removes at least a portion of the water from the first liquid stream to increase the concentration of the dissolved salt to produce a first concentrated brine stream, and
the first concentrated brine stream is discharged from the first fluidic circuit after the first concentrated brine stream reaches a first discharge condition; and

supplying a second liquid stream comprising water and a dissolved salt to a second fluidic circuit comprising a second humidifier, wherein:
the second humidifier removes at least a portion of the water from the second liquid stream to increase the concentration of the dissolved salt to produce a second concentrated brine stream, and
the second concentrated brine stream is discharged from the second fluidic circuit after the second concentrated brine stream reaches a second discharge condition;

wherein the discharge of the second concentrated brine stream from the second fluidic circuit occurs after the discharge of the first concentrated brine stream from the first fluidic circuit.

2. The method of claim 1 , wherein the first discharge condition is a first threshold density of the first concentrated brine stream, the first threshold density being at least 10 pounds per gallon.

3. The method of claim 2 , wherein the second discharge condition is a second threshold density of the second concentrated brine stream, the second threshold density being at least 10 pounds per gallon.

4. The method of claim 1 , wherein the first discharge condition is a first threshold salinity of the first concentrated brine stream, the first threshold salinity being at least 25 wt %.

5. The method of claim 4 , wherein the second discharge condition is a second threshold salinity of the second concentrated brine stream, the second threshold salinity being at least 25 wt %.

6. The method of claim 1 , wherein the first humidifier is a bubble column humidifier.

7. The method of claim 6 , wherein the second humidifier is a bubble column humidifier.

8. The method of claim 1 , wherein the first humidifier is fluidically connected to a first dehumidifier, and the first dehumidifier produces a stream comprising substantially pure water.

9. The method of claim 1 , wherein substantially no solid salt is produced in the first fluidic circuit.

10. The method of claim 1 , wherein substantially no solid salt is produced in the second fluidic circuit.

11. The method of claim 1 , wherein the first humidifier is a packed bed humidifier.

12. The method of claim 6 , wherein the second humidifier is a packed bed humidifier.

13. The method of claim 8 , wherein the second humidifier is fluidically connected to a second dehumidifier, and the second dehumidifier produces a stream comprising substantially pure water.

14. The method of claim 8 , wherein the first dehumidifier is a bubble column dehumidifier.

15. The method of claim 13 , wherein the second dehumidifier is a bubble column dehumidifier.

16. The method of claim 1 , further comprising precipitating at least a portion of the salt from the first concentrated brine stream and/or the second concentrated brine stream.

17. The method of claim 1 , further comprising pre-treating the first liquid stream and/or the second liquid stream to remove at least a portion of at least one scale-forming ion.

18. The method of claim 1 , further comprising pre-treating the first liquid stream and/or the second liquid stream to remove at least a portion of a suspended and/or emulsified immiscible phase.

19. The method of claim 1 , further comprising pre-treating the first liquid stream and/or the second liquid stream to remove at least a portion of suspended solids.

Assignees

• Gradiant Corp

Inventors

• Govindan Prakash Narayan
• St John Maximus G
• Lam Steven
• Zaloudek Mark
• Chehayeb Karim M
• Shah Samar

Classifications

• C02F1/08 Primary

  Thin film evaporation · CPC title

• C02F2103/10

  from quarries or from mining activities · CPC title

• C02F2301/046

  Recirculation with an external loop · CPC title

• B01D17/0205

  by gas bubbles or moving solids · CPC title

• C02F1/5245

  using basic salts, e.g. of aluminium and iron · CPC title