Demulsification and extraction of biochemicals from crude and its fractions using water and subcritical/supercritical carbon dioxide as proton pump with pH tuning without precipitating oil components

Patent metadata

Field	Value
Publication number	US-9562198-B2
Application number	US-201414269667-A
Country	US
Kind code	B2
Filing date	May 5, 2014
Priority date	May 5, 2014
Publication date	Feb 7, 2017
Grant date	Feb 7, 2017

Abstract

A demulsification process for extracting surface active biochemical products from crude oil and its fractions when they are used as feedstock during biochemical productions utilizes subcritical/supercritical CO 2 as a proton pump. The process also includes a pH tuning step, thereby inducing demulsification and precipitation of biochemical products into the aqueous phase, but avoiding asphaltene precipitation by apriori addition of resinous solvents derived from crude oil or bioresources. The biochemical products are then extracted from the aqueous phase via temperature change or some other technique.

First claim

What is claim is:

1. A process for demulsification and extraction of biochemicals from crude oil and its fractions without precipitating other surface active molecules that are part of the crude oil comprising the steps of:
mixing a crude oil emulsion with carbon dioxide from subcritical range to supercritical range to form a mixture, the emulsion containing surface active molecules including aromatic resins, asphaltenes and the biochemicals;
maintaining the mixture at conditions that cause the pH of an aqueous phase of the emulsion to decrease to a first pH value which causes weakening of an interfacial tension of the emulsion; and
maintaining an aromatic resin to asphaltene ratio to be greater than a predefined value such that the asphaltenes are suspended or solvated by the aromatic resins and asphaltene precipitation is prevented, while the biochemicals precipitate or transfer to the aqueous phase and the biochemicals are extracted from the aqueous phase.

2. The process of claim 1 , wherein the crude oil emulsion comprises an emulsion selected from the group consisting of: an oil in water emulsion; a water in oil emulsion; water-in-oil-in-water emulsion; and oil-in-water-in-oil emulsion.

3. The process of claim 1 , wherein the biochemicals comprise rhamnolipids.

4. The process of claim 1 , wherein the surface active molecules comprise molecules having a carboxylic acid group.

5. The process of claim 4 , wherein the surface active molecules include naphthenic acids.

6. The process of claim 4 , wherein the first pH value is below a pH IEP and acid dissociation constants of the carboxylic acid groups of the aromatic resins and asphaltenes.

7. The process of claim 1 , further including the step of allowing the mixture of the crude oil emulsion and the carbon dioxide to stabilize such that the carbon dioxide diffuses across an oil phase of the crude oil emulsion to an emulsion phase boundary and subsequently enters an aqueous phase of the crude oil emulsion.

8. The process of claim 1 , further including the step of introducing a resin supplement from refinery products into the emulsion prior to addition of the carbon dioxide when the aromatic resin to asphaltene ratio is below the predefined value.

9. The process of claim 1 , further including the step of introducing one of: (1) molecules that are derived from bioresources and (2) petroleum fractions prior to addition of the carbon dioxide to maintain the aromatic resin to asphaltene ratio greater than the predefined value.

10. The process of claim 1 , further including the step of maintaining an overall acidic to basic function group ratio between 0.25 to 4.

11. The process of claim 10 , wherein the ratio is maintained between 0.5 and 2.

12. The process of claim 10 , further including the step of adding additional aromatic resins to maintain the overall acidic to basic function group ratio between 0.25 to 4.

13. The process of claim 1 , where the crude oil emulsion is contained in a vessel and a temperature of the crude oil emulsion is above a freezing point of water; a pressure of vessel being maintained between 1 bar to 300 bars; and a temperature of the vessel is above the subcritical-supercritical temperature of carbon dioxide and below 150° C.

14. The process of claim 1 , further including the step of adjusting the pH of the aqueous phase to cause a lowering of a zeta potential, at a phase boundary of the emulsion, to reach near an isoelectric point of the aromatic resin, naphthenic acid and the asphaltenes, thereby causing an interfacial film of the emulsion to weaken.

15. The process of claim 14 , where the zeta potential is lowered to between −10 eV to 10 eV.

16. The process of claim 1 , wherein the asphaltenes are kept solvated in the crude oil emulsion and thereby prevented from precipitating.

17. The process of claim 1 , wherein —COOH groups of the surface active molecules become inactive at the first pH value due to formation of carbonic acid and dissociation thereof to release a proton (H + ) at elevated pressures within a vessel containing the mixture.

18. The process of claim 1 , further including the step of maintaining an overall acidic to basic function group ratio between 0.25 to 4 and maintaining the pH of the aqueous phase below a pK a of the biochemicals, thereby causing the biochemicals to be electrically inactive and allowing precipitation or remain in dissolved form due to the hydrogen bonding with the aqueous phase thereof.

19. A process for demulsification and extraction of biochemicals from crude oil and its fractions comprising the steps of:
mixing a crude oil emulsion with carbon dioxide from subcritical range to supercritical range to form a mixture, the emulsion containing surface active molecules including aromatic resins, asphaltenes and the biochemicals;
maintaining the mixture at conditions that cause the pH of an aqueous phase of the emulsion to decrease to a first pH value which causes weakening of an interfacial tension of the emulsion, thereby causing demulsification to occur; and
maintaining the mixture at conditions that cause the asphaltenes to remain solvated in the crude oil, thereby preventing asphaltene precipitation, while the biochemicals precipitate or transfer to the aqueous phase and the biochemicals are extracted from the aqueous phase.

Assignees

• Saudi Arabian Oil Co

Inventors

• Yusuf Zaki

Classifications

• B01D17/047

  with separation aids · CPC title

• B01D17/044

  by changing the pressure · CPC title

• C10G33/04 Primary

  with chemical means · CPC title