Method of removing water and contaminants from crude oil containing same

• US 20020079248A1
• Filed: 12/11/2001
• Published: 06/27/2002
• Est. Priority Date: 06/27/2000
• Status: Active Grant

• Current Assignee: Worleyparsons Canada Pty Limited
• Original Assignee: Colt Engineering Corporation (Worley Ltd.)
• Inventors: Kresnyak, Steve
• Granted Patent: US 6,849,175 B2
• Time in Patent Office: Days
• US Class Current: 208/187
• CPC Class Codes: C10G 33/00 Dewatering or demulsification of hydrocarbon oils by distillation C10G7/04

Abstract

A method for contaminant and water removal from crude oil. The method involves recirculating at least a portion of the dewatered crude into a dehydrator. The dehydrator contains a heated dehydrated crude oil and the surface or adjacent thereto is maintained at a temperature sufficient to vaporize any water contacting the surface from crude oil to be treated in the dehydrator. It has been found important to maintain a substantially uniform temperature at or below the vaporizing surface in order to effectively treat crude oil for dewatering purposes. Significant temperature fluctuations are typically realized by dehydrators since heat enthalpy is removed in order to vaporize the water in the crude oil. Such fluctuations lead to process complications and upset and are therefore undesirable. The instant invention recognizes this limitation and substantially reduces foaming and provides for a smoothly running and efficient dehydration process.

Claims

1. A method of removing water and solids from crude oil containing water and solids, comprising:

a dehydration phase and a separation phase, said dehydration phase including;

providing a source of crude oil containing water;

providing a dehydrator for dehydrating said crude oil containing water, said dehydrator having an inlet and an outlet and a vaporizing surface of dry crude oil at temperatures sufficient to vaporize water contacting said surface;

exposing said source of crude oil to said dry crude;

vaporizing said water in said source;

said separation phase including;

isolating within said dehydrator solids present in dehydrated crude from said dehydrated crude; and

re-circulating at least a portion of dehydrated and solid separated crude for contact with at least one of said dehydrator or said source of crude oil for maintaining a substantially uniform temperature at said vaporizing surface.

2. The method as defined in claim 1, wherein said solids are isolated by gravity separation within said separator.

3. The method as defined in claim 2, wherein said solids are isolated by mechanical agitation within said separator.

4. The method as defined in claim 1, wherein isolation of said solids further includes at least one or a combination of filtering, hydrocycloning, centrifuging said dehydrated crude prior to re-circulation in said dehydrator.

5. The method as defined in claim 1, further including the step of collecting gaseous components from said vaporizing and condensing said components.

6. The method as defined in claim 1, further including the step of regulating heat content of said dehydrated crude re-circulated with heating means.

7. The method as defined in claim 5, further including the step of collecting gaseous components from vaporizing in said dehydrator with distillation means.

8. The method as defined in claim 1, wherein in said dehydrated crude has a basic sediment water content of less than 0.5% by volume water.

9. The method as defined in claim 1, wherein said source of crude oil contains greater than 5% by volume water.

10. A method of removing water and solids from a crude oil containing water and solids, comprising:

a dehydration phase and a separation phase, said dehydration phase including;

providing a source of crude oil containing water;

providing a dehydrator for dehydrating said crude oil, said dehydrator having an inlet and an outlet and a vaporizing surface of dry crude oil at a temperature sufficient to vaporize water contacting said surface;

contacting said source and said dry crude oil to flash water from said source to thereby remove said water from said source;

said separation phase including;

isolating within said dehydrator solids present in dehydrated crude from said dehydrated crude;

re-circulating said dehydrated crude oil for contact immediately below said vaporizing surface; and

re-circulating said dehydrated crude oil for mixing with said source of crude oil, whereby said vaporizing surface is selectively heated to return heat energy lost from flash evaporating water from said source.

11. The method as defined in claim 10, further including a step of collecting and condensing light hydrocarbon fluid.

12. The method as defined in claim 11, wherein collected and condensed light hydrocarbon fluid is collected and condensed with distillation means.

13. The method as defined in claim 12, further including the step of re-circulating condensed light hydrocarbon fluid to said source of crude oil.

14. The method as defined in claim 11, further including the step of diluting said source of crude oil with condensed light hydrocarbon fluid.

15. The method as defined in claim 10, wherein said light hydrocarbon fluid. heating is provided by at least one of re-circulating dehydrated crude oil into said dry crude oil and re-circulating dry dehydrated crude oil into contact with said source of crude oil.

16. The method as defined in claim 10, wherein said solids are isolated by at least one of gravity separation and mechanical agitation within said separator.

18. The method as defined in claim 17, further including the step of re-circulating at least a portion of dehydrated and solid separated crude for contact with at least one of said dehydrator or said source of crude oil for maintaining a substantially uniform temperature at said vaporizing surface.

19. The method as defined in claim 18, further including the step of re-circulating said dehydrated crude oil for contact immediately below said vaporizing surface whereby said vaporizing surface is selectively heated to return heat energy lost from flash evaporating water from said source.

20. The method as defined in claim 17, further including the step of upgrading said dehydrated crude oil from between 7 API and 10 API to 21 API.

21. The method as defined in claim 17, further including the step of upgrading said dehydrated crude oil by unit operations selected from the group consisting of visbreaking, hydro processing, thermal cracking and distillation.

22. The method as defined in claim 17, wherein said dehydrated crude has a viscosity of 350 Cst at 10 celcius.

23. The method as defined in claim 17, further including the step of collecting gaseous components from vaporizing in said dehydrator with distillation means.

24. The method as defined in claim 23, further including the step of recycling condensed gaseous components for dilution of said effluent.

25. The method as defined in claim 17, further including the step of providing a diluent makeup stream for contact with said effluent prior to pretreating.

17. A method of upgrading effluent containing crude oil to dehydrated crude oil, comprising:

a conditioning phase, a dehydration phase, and a separation phase, said conditioning phase including;

providing a source of effluent at least containing crude oil with water entrained therein and solids;

pretreating said effluent to remove at least some of said water and solids to thereby concentrate the crude oil;

said dehydration phase including;

providing a dehydrator for dehydrating said crude oil, said dehydrator having an inlet and an outlet and a vaporizing surface of dry crude oil at temperatures sufficient to vaporize water contacting said surface;

exposing said crude oil to said dry crude;

vaporizing said water in said crude oil to dehydrate said crude oil; and

said separation phase including;

isolating within said dehydrator solids present in dehydrated crude to form clean dehydrated crude oil.