Process for the purification of a glycol solution

• US 5,817,889 A
• Filed: 08/07/1995
• Issued: 10/06/1998
• Est. Priority Date: 10/29/1993
• Status: Expired due to Fees

• Current Assignee: ELF Exploration Production (Cook Composites and Polymers)
• Original Assignee: ELF Aquitaine Production
• Inventors: Blanc, Claude, Morin, Daniel, Pondebat, Chantal
• Primary Examiner(s): Burn, Brian M.
• Assistant Examiner(s): PADMANABHAN, SREENIVASAN
• Application Number:
  US08/464,720
• Time in Patent Office: 1,156 Days
• Field of Search: 568/679, 568/680, 568/868
• US Class Current: 568/679
• CPC Class Codes: C07C 29/86 by liquid-liquid treatment
• CPC Class Codes: C07C 31/20 Dihydroxylic alcohols
• CPC Class Codes: C07C 41/38 by liquid-liquid treatment
• CPC Class Codes: C07C 43/11 Polyethers containing —O—(C—C—O—)n units with ≤ 2 n≤ 10
• CPC Class Codes: C10L 2290/12 Regeneration of a solvent, catalyst, adsorbent or any other component used to treat or prepare a fuel
• CPC Class Codes: C10L 2290/543 Distillation, fractionation or rectification for separating fractions, components or impurities during preparation or upgrading of a fuel
• CPC Class Codes: C10L 3/106 of water
• CPC Class Codes: C10L 3/107 Limiting or prohibiting hydrate formation

Abstract

An amount of water is added to a glycol solution to be purified to enable segregation of the resulting mixture into a hydrocarbon phase and a glycol phase. The hydrocarbon phase is separated from the glycol phase and said glycol phase is desalted, e.g. by electrodialysis, to give a desalted and substantially hydrocarbon-free glycol solution which is then concentrated by steam stripping. The method is useful for purifying waste glycol solutions resulting from oil or gas production effluent processing using glycols, and in particular from a gas hydrate inhibition treatment or natural gas dehydration.

Claims

1. A process for the purification of glycol solutions based on one or more glycols and containing water and, as impurities, dissolved salts, which are dissociated as anions and cations, and hydrocarbons in at least one of the dissolved and emulsified states, said process consisting essentially of

a) incorporating into the glycol solution to be purified an amount of water which allows demixing of the resulting mixture into a hydrocarbon phase consisting of virtually all of the hydrocarbons present in said glycol solution to be purified, and into a glycol phase, formed of the other constituents of the glycol solution and the added water;

b) separating the glycol phase from the hydrocarbon phase; and

c) subjecting the separated glycol phase to a desalting treatment for elimination of the salts dissolved in said glycol phase by making use of a technique for the selective separation of the anions and cations of said salts, with production of a purified glycol solution having a low hydrocarbon content and a controlled salt content.

2. A process according to claim 1, wherein the glycol solution to be purified contains a hydrocarbon content of less than 20% by weight.

3. A process according to claim 1, wherein the glycol or glycols present in the glycol solution to be purified correspond to the general formula HO(C_n H_2n O)_p --C_n H₂ OH, where n is an integer ranging from 2 to 4, and p represents 0 or an integer ranging from 1 to 4.

4. A process according to claim 1, wherein the glycol or glycols present in the glycol solution to be purified are selected from the group consisting of monoethylene glycol (MEG), diethylene glycol (DEG), triethylene glycol (TEG) and propylene glycol.

5. A process according to claim 1, the amount of water which is added to the glycol solution to be purified, in order to obtain demixing of the mixture into the hydrocarbon phase and the glycol phase, is such that the quotient α

of the water;

hydrocarbons volume ratio, in the glycol solution after addition of the water required for demixing, to the water;

hydrocarbons volume ratio, in the glycol solution to be purified before addition of the water for demixing, is between 1 and 15.

6. A process according to claim 5, wherein the glycol solution to be purified is based on MEG and/or DEG and wherein d is 1<

α

<

2.

7. A process according to claim 5, wherein the glycol solution to be purified is based on TEG and that α

is such that 5<

α

<

10.

8. A process according to claim 1 the addition of water to the glycol solution to be purified, resulting in demixing of the resulting mixture into the hydrocarbon phase and the glycol phase, and the separation of the said phases are performed at temperatures below about 60°

C.

9. A process according to claim 1 the glycol phase arising from the demixing is subjected to a filtration before being brought to the desalting treatment, in order to remove solid particles whose mean diameter is greater than about 10 μ

m.

10. A process according to claim 1 the treatment for desalting the substantially hydrocarbon-free glycol phase is performed by percolation of the glycol solution to be desalted through one or more beds of ion exchange materials which selectively bind the anions or the cations respectively.

11. A process according to one of claims 1 to 9 characterized in that the treatment for desalting the substantially hydrocarbon-free glycol phase is performed by electrodialysis through membranes which are alternately selectively permeable to anions and to cations.

12. A process according to claim 1 the glycol solution arising from the desalting treatment is subjected to concentration by stripping using steam and optionally an extra gas.

13. A process according to claim 12, wherein the steps of demixing, desalting and concentration are performed continuously.

14. A process according to claim 12, wherein the steps of demixing and of concentration are performed continuously and the step of desalting is carried out intermittently.

15. A process according to claim 13, wherein desalting is performed by electrodialysis carried out with a DC electric current of constant intensity I and such that the current density, that is to say the ratio of the intensity I to the surface area of one of the electrodialysis membranes, is between 0.1 and 450 A/m².

16. A process according to claim 14, wherein the desalting is performed by electrodialysis carried out with a DC electric current, for which the mean value Im of the intensity, over the duration of the treatment, is such that the current density, that is wherein the ratio of the mean intensity Im to the surface area of one of the electrodialysis membranes, is between 0.1 and 450 A/m².

17. A process according to claims 15 or 16, wherein the glycol phase to be desalted contains a glycol consisting respectively of MEG, DEG and TEG and wherein the electrodialysis is performed with a current density between 0.1 and 150 A/m², 0.1 and 300 A/m² and 0.1 and 450 A/m² respectively.

18. A process according to claim 1 the glycol solution to be purified arises from the treatment of petroleum or gas production effluents by glycols.

19. A process according to claim 1 the glycol solution to be purified arises from the treatment, by glycols, for prevention of the formation of gas hydrates in the discharge pipes of multiphase effluents from petroleum or gas production.

20. A process according to claim 1, characterized in that the glycol solution to be purified is a used glycol solution arising from the treatment for dehydration of natural gases by glycols or a regenerated glycol solution arising from the concentration by stripping, using steam and optionally an extra gas, of such a used glycol solution.

21. The process according to claim 3 wherein the glycol possesses less than 7 carbon atoms in the molecule.

22. The process according to claim 5 wherein the quotient α

is between 1 and 10.