IP Library Granted Patent US 8,702,993
Granted Patent B2
US 8,702,993 · App. 11/298,936 · Granted Apr 22, 2014

Amine-aldehyde resins and uses thereof in separation processes

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Quick Facts
Patent No.
US 8,702,993
App. No.
11/298,936
Granted
Apr 22, 2014
Kind
B2
Abstract

Amine-aldehyde resins are disclosed for removing a wide variety of solids and/or ionic species from the liquids in which they are suspended and/or dissolved. These resins are especially useful as froth flotation depressants in the separation of bitumen from sand and/or clay or in the beneficiation of clay (e.g., kaolin clay) from an impure clay-containing ore. The resins are also useful for treating aqueous liquid suspensions to remove solid particulates, as well as for removing metallic ions in the purification of water.

Claims (30)

1. A method for purifying an aqueous liquid suspension, comprising:

treating a liquid suspension comprising clay with a urea-formaldehyde resin having a formaldehyde to urea molar ratio of about 1.5:1 to about 4:1, wherein an alkaline reaction condition is maintained throughout the synthesis of the urea-formaldehyde resin; and

removing, either after or during the treating step, a purified liquid or at least a portion of the clay by sedimentation or floatation.

2. The method of claim 1 , wherein treating the liquid suspension comprises flocculating the clay.

3. The method of claim 1 , wherein at least a portion of the clay is removed by sedimentation.

4. The method of claim 1 , wherein the liquid suspension is from a phosphate production facility.

5. The method of claim 4 , wherein the purified water is removed for reuse in phosphate production.

6. The method of claim 1 , wherein the urea-formaldehyde resin is modified with one or more anionic functional groups.

7. The method of claim 1 , wherein the urea-formaldehyde resin is stabilized by reacting with an alcohol comprising ethanol, n-propanol, isopropanol, n-butanol, or isobutanol.

8. The method of claim 1 , wherein the urea-formaldehyde resin has a concentration of free formaldehyde of less than 1%, based on the total weight of the urea-formaldehyde resin.

9. The method of claim 1 , wherein the urea-formaldehyde resin is formed by reacting a monomer mixture consisting essentially of urea and formaldehyde.

10. The method of claim 1 , wherein the urea-formaldehyde resin has a number average molecular weight (Mn) of about 400 grams per mole to about 1,200 grams per mole.

11. The method of claim 1 , wherein the urea-formaldehyde resin has a concentration of free formaldehyde of less than 1%, based on the total weight of the urea-formaldehyde resin, the urea-formaldehyde resin has a number average molecular weight (Mn) of about 400 grams per mole to about 1,200 grams per mole, and the urea-formaldehyde resin is stabilized by reacting with an alcohol comprising ethanol, n-propanol, isopropanol, n-butanol, or isobutanol.

12. A method for purifying an aqueous liquid suspension, comprising:

treating a liquid suspension comprising a solid contaminant with a generally cationic urea-formaldehyde resin having a formaldehyde to urea molar ratio of about 1.5:1 to about 4:1, wherein an alkaline reaction condition is maintained throughout the synthesis of the urea-formaldehyde resin; and

removing, either after or during the treating step, a purified liquid or at least a portion of the solid contaminant by sedimentation or floatation.

13. The method of claim 12 , wherein treating the liquid suspension comprises flocculating the solid contaminant.

14. The method of claim 12 , wherein at least a portion of the solid contaminant is removed by sedimentation.

15. The method of claim 12 , wherein the liquid suspension is from a phosphate production facility.

16. The method of claim 15 , wherein the purified water is removed for reuse in phosphate production.

17. The method of claim 12 , wherein the solid contaminant comprises sand, clay, or a combination thereof.

18. The method of claim 17 , wherein the liquid suspension is a clay-containing effluent slurry from a phosphate production facility.

19. The method of claim 12 , wherein the urea-formaldehyde resin is etherified with an alcohol selected from the group consisting of: ethanol, n-propanol, isopropanol, n-butanol, and isobutanol.

20. The method of claim 12 , wherein the at least a portion of the solid contaminant is removed by floatation.

21. The method of claim 20 , wherein the floatation comprises froth floatation.

22. The method of claim 12 , wherein the urea-formaldehyde resin has a number average molecular weight ranging from about 400 grams per mole to about 1,200 grams per mole.

23. The method of claim 12 , wherein the urea-formaldehyde resin is formed by reacting a monomer mixture consisting essentially of urea and formaldehyde.

24. The method of claim 12 , wherein the urea-formaldehyde resin has a concentration of free formaldehyde of less than 1%, based on the total weight of the urea-formaldehyde resin.

25. The method of claim 12 , wherein the urea-formaldehyde resin has a concentration of free formaldehyde of less than 1%, based on the total weight of the urea-formaldehyde resin, the urea-formaldehyde resin has a number average molecular weight (Mn) of about 400 grams per mole to about 1,200 grams per mole, and the urea-formaldehyde resin is stabilized by reacting with an alcohol comprising ethanol, n-propanol, isopropanol, n-butanol, or isobutanol.

26. The method of claim 12 , wherein the urea-formaldehyde resin has a formaldehyde to urea molar ratio of about 2:1 to about 3:1, the urea-formaldehyde resin has a concentration of free formaldehyde of less than 1%, based on the total weight of the urea-formaldehyde resin, the urea-formaldehyde resin is stabilized by reacting with an alcohol comprising ethanol, n-propanol, isopropanol, n-butanol, or isobutanol, and the urea-formaldehyde resin is formed by reacting a monomer mixture consisting essentially of urea and formaldehyde or a monomer mixture consisting essentially of urea, formaldehyde, and ammonia.