Preparation of rare earth metals and other chemicals from industrial waste coal ash

Patent metadata

Field	Value
Publication number	US-11866804-B2
Application number	US-202117536403-A
Country	US
Kind code	B2
Filing date	Nov 29, 2021
Priority date	Nov 20, 2017
Publication date	Jan 9, 2024
Grant date	Jan 9, 2024

Abstract

A process for the isolation and purification of substantially pure chemicals, including silica gel, sodium silicate, aluminum silicate, iron oxide, and rare earth elements (or rare earth metals, REEs), from massive industrial waste coal ash including a plurality of caustic extractions of coal ash at an elevated temperature, followed by an acidic treatment to dissolve aluminum silicate and REEs. Dissolved aluminum silicate is precipitated out by pH adjustment as a solid product while REEs remain in the solution. REEs are captured and enriched using an ion exchange column. Alternatively, the solution containing aluminum silicate and REEs is heated to produce silica gel, which is separated from the enriched REEs solution. REEs are then isolated and purified from the enriched solution to afford substantially pure individual REE by a ligand-assisted chromatography.

First claim

What is claimed is:

1. A process for preparing pure chemicals from coal ash, the process comprising:
a. extracting coal ash with a first caustic solution at a temperature elevated above ambient;
b. separating undissolved solid residue from said first caustic extracting solution, wherein said first caustic extracting solution is stored for later processing and said solid residue is washed with water;
c. treating the water washed solid residue with a first acid, wherein pH of the resulting acidic solution is maintained at about 3 and then the leftover solid is separated and washed with water;
d. extracting the water washed solid with a second caustic solution at a temperature elevated above ambient;
e. separating undissolved solid residue from the second caustic extracting solution and washing with water wherein said second caustic extracting solution is stored for later processing;
f. treating the undissolved solid residue with a second acid to bring the pH of the resulting acidic solution to about 3, and isolating the leftover solid as a purified iron oxide with aluminum silicate;
g. combining the acidic extraction solutions from steps c and f, and adjusting the pH to about 5 with a base whereby aluminum silicate precipitates out from the solution as a product and the leftover solution contains enriched rare earth elements (REEs); and
h. combining the first and the second caustic extracting solutions to recover purified sodium silicate by pH adjustment with ana third acid, wherein at least one respective caustic extraction solution includes sodium hydroxide and wherein at least one respective caustic extraction solution includes potassium hydroxide.

2. The process of claim 1 further comprising steps of isolation and purification of each individual REE from said leftover acid extraction solution by a ligand-assisted chromatography comprising
a. enriching by capturing said REEs on an ion exchange column;
b. eluting REEs from said ion exchange column with a chelating ligand;
c. binding said chelating ligand solution of REEs to an absorbent column;
d. eluting individual REE with an isocratic or gradient of a ligand;
e. combining respective fractions of respective pure individual REE separately; and
f. recovering individual REE from the combined fractions.

3. The process of claim 2 wherein the chelating ligand is EDTA salt and further comprising a step of precipitating and recycling EDTA salt.

4. The process of claim 1 , wherein the coal ash is fly ash.

5. The process of claim 1 , wherein the second caustic extracting solution is the solution from the first caustic extraction.

6. The process of claim 1 , wherein the concentration of at least one respective caustic extracting solution is from about 1 M to about 15 M.

7. The process of claim 1 , wherein at least one respective acid is hydrochloric acid, sulfuric acid, or nitric acid.

8. The process of claim 1 , wherein the concentration of at least one respective acid is from about 0.01 M to about 12 M.

9. The process of claim 1 , wherein the temperature elevated above ambient is from about 50° C. to about 250° C.

10. The process of claim 1 , wherein the mass ratio of coal ash to base of at least one respective caustic extraction solution is from about 1:1 to about 1:10.

11. The process of claim 1 , wherein said sodium silicate from caustic extraction is acidified to afford silica gel.

12. A process for preparing pure chemicals from coal ash, the process comprising:
a. extracting coal ash with a caustic solution at a temperature elevated above ambient;
b. separating undissolved solid residue from said caustic extraction solution and washing said undissolved solid residue with water;
c. treating the water washed solid residue with an acid at a mass ratio of solid to acid about 1:10 and then separating leftover solid to afford an acidic extraction solution;
d. loading the acidic extraction solution to a cation exchange column and collecting the pass-through eluent;
e. treating the pass-through eluent with a base to pH about 3, at which point iron hydroxide precipitates out and is isolated; then bringing the pH of the solution up to about 8 whereby aluminum hydroxide precipitates out and is isolated; and
f. eluting the loaded cation exchange column first with a solution of sodium chloride to afford fractions containing aluminum and iron, and then with a solution of a chelating ligand to afford fractions of enriched REEs;
wherein the caustic extraction solution includes both sodium hydroxide and potassium hydroxide.

13. The process of claim 12 further comprising steps of isolation and purification each individual REE from said fractions of enriched REEs, the steps comprising
a. capturing said REEs on an ion exchange column,
b. eluting REEs from said ion exchange column with a chelating ligand,
c. binding said chelating ligand solution of REEs to an absorbent column,
d. eluting individual REE with an isocratic or gradient of a ligand,
e. combining respective fractions of respective pure individual REE separately, and
f. recovering individual REE from the combined fractions.

14. The process of claim 13 wherein the chelating ligand is EDTA salt and further comprising a step of precipitating and recycling EDTA salt.

15. The process of claim 12 further comprising a step of washing coal ash with acid to remove calcium oxide and other salts of alkali earth metals before extracting with a caustic solution at a temperature elevated above ambient.

16. The process of claim 12 further comprising a step of exposing the leftover solid from acid extraction to a magnetic field and collecting materials attracted to said magnetic field as an iron-enriched product.

17. The process of claim 12 further comprising a step of acidifying said caustic extraction solution to afford silica gel.

18. The process of claim 12 , wherein the caustic extracting solution has a concentration from about 1 M to about 15 M.

19. The process of claim 12 , wherein the acidic extraction solution is made of an acid selected from the group consisting of hydrochloric acid, sulfuric acid, and nitric acid.

20. The process of claim 12 , wherein the acidic extraction solution has a concentration from about 0.1 M to about 12 M.

21. The process of claim 12 , wherein said temperature elevated above ambient is from about 50° C. to about 250° C.

Assignees

• Purdue Research Foundation

Inventors

• Wang Nien-Hwa Linda
• Choi Hoon
• Harvey David

Classifications

• C22B7/007 Primary

  by acid leaching · CPC title

• C01B33/14 Primary

  Colloidal silica, e.g. dispersions, gels, sols · CPC title

• C01B33/26

  Aluminium-containing silicates {, i.e. silico-aluminates} · CPC title

• C01B33/32

  Alkali metal silicates ({C01B33/24} , C01B33/26 take precedence) · CPC title

• C01F7/0693

  from waste-like raw materials, e.g. fly ash or Bayer calcination dust · CPC title