Purification of barium values

• US 4,834,952 A
• Filed: 03/02/1987
• Issued: 05/30/1989
• Est. Priority Date: 02/28/1986
• Status: Expired due to Fees

• Current Assignee: Rhone-Poulenc Chimie
• Original Assignee: Rhone-Poulenc Chimie
• Inventors: Sabot, Jean-Louis, Rollat, Alain
• Primary Examiner(s): Stoll, Robert L.
• Application Number:
  US07/020,363
• Time in Patent Office: 820 Days
• Field of Search: 423/157, 423/635, 423/DIG. 14, 423/395, 423/497, 423/430, 423/165, 75/101 BE, 75/121, 75/108, 210/688, 210/685, 210/673
• US Class Current: 423/157
• CPC Class Codes: C01F 11/005 Preparation involving liquid-liquid extraction, absorption or ion-exchange
• CPC Class Codes: C01F 11/188 Barium carbonate
• CPC Class Codes: C01F 11/32 Purification
• CPC Class Codes: C01F 11/44 Concentrating; Crystallisating; Dehydrating; Preventing the absorption of moisture or caking
• CPC Class Codes: C01P 2006/80 Compositional purity
• CPC Class Codes: C22B 3/32 Carboxylic acids
• CPC Class Codes: C22B 3/364 Quinoline
• CPC Class Codes: C22B 3/3844 Phosphonic acid, e.g. H2P(O)(OH)2
• CPC Class Codes: C22B 3/408 using a mixture of phosphorus-based acid derivatives of different types
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

Purified barium salts essentially devoid of strontium impurities, e.g., highly pure barium carbonate, are produced by liquid/liquid extracting an aqueous solution of impure barium values with an organic solvent medium which comprises at least one water-insoluble carboxylic acid, phosphonic acid monoester, or substituted 8-hydroxyquinoline extractant. The mixture of extraction is separated into a purified aqueous phase containing the desired barium salt values and an organic phase containing the impurity values sought to be removed.

Claims

1. A process for the production of a purified barium salt essentially devoid of strontium impurities, comprising extracting an aqueous solution of impure barium values with an organic solvent medium which comprises at least one of the following substantially water-insoluble organic extractants:

(i) a carboxylic acid having the following general formula (I);

##STR11## in which R₁ and R₂ are straight or branched chain alkyl radicals, or substituted such alkyl radicals, with the proviso that the total number of carbon atoms present in said two radicals is at least equal to 6;

(ii) a phosphonic acid monoester having the following general formula (II);

##STR12## in which R'"'"'₁ and R'"'"'₂ are straight or branched chain, nonhalogenated alkyl or alkenyl radicals;

(iii) an 8-hydroxyquinoline having the following general formula (III);

##STR13## in which R₃, R₄, R₅, R`hd 6, R₇ and R₈, which may be identical jor different, are each hydrogen, or a substituted or unsubstituted alkyl, alkenyl, alicyclic or aromatic radical, with the proviso that R₃, R₄, R₅, R₆, R₇ and R₈ may not all be hydrogen at the same time;

separating the mixture of extraction into a purified aqueous phase comprising the desired barium salt values and an organic phase comprising those impurity values sought to be removed; and

thence recovering said purified aqueous phase.

2. The process as defined by claim 1, further comprising recovering purified barium salt values from said purified aqueous phase.

3. The process as defined by claim 1, said organic solvent medium comprising at least one extractant having the formula (I).

4. The process as defined by claim 1, said organic solvent medium comprising at least one extractant having the formula (II).

5. The process as defined by claim 4, wherein said extractant having the formula (II), R'"'"'₁ and R'"'"'₂ are alkyl radicals.

6. The process as defined by claim 5, said extractant comprising (2-ethylhexyl) (2-ethylhexyl) phosphonic acid.

7. The process as defined by claim 1, said organic solvent medium comprising at least one extractant having the formula (III).

8. The process as defined by claim 7, wherein said extractant having the formula (III), R₃, R₄, R₅, R₆, R₇ and R₈ are either hydrogen or an alkyl radical with the proviso that R₃, R₄, R`hd 5, R₆, R₇ and R₈ may not all by hydrogen at the same time.

9. The process as defined by claim 8, wherein said extractant having the formula (III), R₃ is an alkyl radical.

10. The process as defined by claim 9, wherein R₃ is undecyl.

11. The process as defined by claim 9, wherein R₃ is 1-methyl-4-ethyloctyl.

12. The process as defined by claim 1, said organic solvent medium comprising at least one diluent.

13. The process as defined by claim 12, said at least one diluent comprising a saturated or unsaturated aliphatic hydrocarbon, an aromatic hydrocarbon, or mixture thereof.

14. The process as defined by claim 13, said at least one diluent comprising kerosene.

15. The process as defined by claim 1, said organic solvent medium comprising at least one modifier therefor to reduce separation of components of the solvent under acidic condition.

16. The process as defined by claim 15, said at least one modifier comprising a substantially water-insoluble alcohol.

17. The process as defined by claim 3, the equilibrium mixture of extraction having a pH of from 5 to 9.

18. The process as defined by claim 3, the equilibrium mixture of extraction having a pH of from 7 to 8.

19. The process as defined by claim 4, the equilibrium mixture of extraction having a pH of form 2 to 6.

20. The process as defined by claim 4, the equilibrium mixture of extraction having a pH of from 4 to 5.

21. The process as defined by claim 7, the equilibrium mixture of extraction having a pH of greater than 10.

22. The process as defined by claim 7, the equilibrium mixture of extraction having a pH of from 11 to 13.

23. The process as defined by claim 1, carried out continuously and countercurrently.

24. The process as defined by claim 1, further comprising back extracting said separated organic phase with an aqueous acid solution and separating the mixture of back-extraction into a purified organic phase and an impure aqueous phase.

25. The process as defined by claim 24, further comprising recycling said purified organic phase to said starting aqueous solution of impure barium values.

26. The process as defined by claim 1, said starting aqueous solution of impure barium values comprising barium nitrate.

27. The process as defined by claim 26, comprising adding ammonium bicarbonate to said purified aqueous phase, whereby a precipitate of purified barium carbonate is produced.

28. The process as defined by claim 1, said starting aqueous solution of impure barium values comprising barium chloride.

29. The process as defined by claim 1, said starting aqueous solution of impure barium values comprising hydrated barium hydroxide.

30. The process as defined by claim 29, said starting aqueous solution of impure barium values comprising octahydrated barium hydroxide.