IP Library Granted Patent US 9,051,827
Granted Patent B1
US 9,051,827 · App. 12/823,000 · Granted Jun 9, 2015

Selective removal of silica from silica containing brines

Inventor: Stephen Harrison (Benicia, CA)
Assignee: Simbol Mining Corporation
E21B43/16E21B43/25
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Quick Facts
Patent No.
US 9,051,827
App. No.
12/823,000
Granted
Jun 9, 2015
Kind
B1
Abstract

A method for selective removal and recovery of silica and silicon containing compounds from solutions that include silica and silicon containing compounds, including geothermal brines. Also included are methods of preventing silica scale buildup in the geothermal power equipment and processes employing geothermal brines by the selective removal of silica.

Claims (27)

1. A method for preventing silica scale in geothermal brine reinjection wells by selectively removing silica from a geothermal brine solution, the method comprising the steps of:

obtaining a geothermal brine solution comprising silica;

maintaining the pH of the geothermal brine solution at a pH of between 4 and 6.25;

contacting the geothermal brine solution comprising silica with activated alumina, such that silica present in the geothermal brine solution selectively binds to the activated alumina;

recovering an aqueous brine product stream from the contacting step, said aqueous product stream having a reduced silica concentration relative to the geothermal brine solution; and

injecting the aqueous brine product stream into the geothermal well, the aqueous brine product stream comprising less than about 80 ppm of silica.

2. The method of claim 1 , wherein the aqueous brine product stream comprises less than about 35 ppm of silica.

3. The method of claim 1 , wherein the aqueous brine product stream comprises less than about 20 ppm of silica.

4. The method of claim 1 , wherein the aqueous brine product stream comprises less than about 10 ppm of silica.

5. The method of claim 1 , wherein the geothermal brine solution comprising silica has a silica concentration of between about 150 ppm and 250 ppm.

6. The method of claim 1 , wherein the geothermal brine solution is contacted with the activated alumina at a temperature of less than about 100° C.

7. The method of claim 1 , further comprising a step prior to injecting the aqueous brine product stream, of supplying at least a portion of the aqueous brine product stream to a process for recovery of lithium.

8. The method of claim 1 , further comprising a step prior to injecting the aqueous brine product stream, of supplying at least a portion of the aqueous brine product stream to a process for recovery of manganese or zinc.

9. A method for preventing silica scale in geothermal brine reinjection wells by selectively removing silica from a geothermal brine solution, the method comprising the steps of:

obtaining a geothermal brine solution containing silica and an iron (II) salt;

oxidizing the iron (II) salt to iron (III) hydroxide;

maintaining the pH of the geothermal brine solution at an adjusted pH of between 4.5 and 6.5;

contacting the silica and the iron (III) hydroxide at the adjusted pH for a time sufficient for the silica to attach to the iron (III) hydroxide and form a solid fraction containing a silica/iron precipitate and a liquid fraction, wherein the liquid fraction contains a geothermal brine product stream having a decreased concentration of silica and iron relative to the geothermal brine;

separating the silica/iron precipitate from the liquid fraction; and

injecting the liquid fraction into the geothermal well, the liquid fraction comprising less than about 80 ppm of silica.

10. The method of claim 9 , wherein the liquid fraction comprises less than about 35 ppm of silica.

11. The method of claim 9 , wherein the liquid fraction comprises less than about 20 ppm of silica.

12. The method of claim 9 , wherein the liquid fraction comprises less than about 10 ppm of silica.

13. The method of claim 9 , wherein the liquid fraction further comprises less than about 15 ppm of iron.

14. The method of claim 9 , wherein the liquid fraction comprises less than about 10 ppm of silica and less than about 10 ppm of iron.

15. The method of claim 9 , further comprising a step prior to injecting the liquid fraction, of supplying at least a portion of the liquid fraction to a process for recovery of lithium.

16. The method of claim 9 , wherein the geothermal brine comprising silica has a silica concentration of between about 150 ppm and 250 ppm.

Assignments (10)
LICENSE Recorded Mar 23, 2023
From: TERRALITHIUM LLC
To: ENERGYSOURCE MINERALS LLC
Reel/Frame 063153/0792 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 26, 2020
From: ALL AMERICAN LITHIUM LLC
To: TERRALITHIUM LLC
Reel/Frame 052749/0324 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 22, 2019
From: ALL AMERICAN LITHIUM LLC
To: TERRALITHIUM LLC
Reel/Frame 050795/0658 →
CHANGE OF NAME Recorded Apr 9, 2019
From: ALGER ALTERNATIVE ENERGY LLC
To: ALL AMERICAN LITHIUM LLC
Reel/Frame 050124/0185 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 27, 2017
From: SIMBOL, INC.
To: ALGER ALTERNATIVE ENERGY, LLC
Reel/Frame 043117/0923 →
RELEASE OF SECURITY INTEREST Recorded Jul 17, 2017
From: GEOTHERMAL ENERGY PROJECT, LLC
To: SIMBOL, INC.
Reel/Frame 043022/0797 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 23, 2014
From: SIMBOL MINING CORP.
To: SIMBOL INC.
Reel/Frame 033158/0528 →
SECURITY INTEREST Recorded Apr 18, 2014
From: SIMBOL, INC.
To: GEOTHERMAL ENERGY PROJECT, LLC
Reel/Frame 032705/0714 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 23, 2013
From: SIMBOL MINING CORP.
To: SIMBOL, INC.
Reel/Frame 029678/0459 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 6, 2010
From: HARRISON, STEPHEN
To: SIMBOL MINING CORPORATION
Reel/Frame 024636/0066 →
Continuity (1)
Provisional Application 61239275 · Sep 2, 2009