Method of removing water and contaminants from crude oil containing same

• US 6,372,123 B1
• Filed: 06/27/2000
• Issued: 04/16/2002
• Est. Priority Date: 06/26/2000
• Status: Expired due to Term

• Current Assignee: Worleyparsons Canada Pty Limited
• Original Assignee: Colt Engineering Corporation (Worley Ltd.)
• Inventors: Shaw, Fred, Kresnyak, Steve
• Primary Examiner(s): NORTON, NADINE GEORGIANNA
• Application Number:
  US09/604,577
• Time in Patent Office: 658 Days
• Field of Search: 208/187
• 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 from crude oil containing water, comprising of steps of:

a) providing a source of crude oil containing water;

b) 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;

c) exposing said source of crude oil to said dry crude;

d) vaporizing at least a portion of said water in said source;

e) re-circulating at least a portion of dehydrated crude; and

f) contacting re-circulated dehydrated crude with said source of crude oil immediately below said vaporizing surface for maintaining a substantially uniform temperature of said vaporizing surface.

2. The method as defined in claim 1, wherein said temperature is a flash evaporating temperature for water.

3. The method as defined in claim 1, including pre-conditioning said source for removal of solids and minerals.

4. The method as defined in claim 1, including pre-conditioning with separation means for separating said solids and minerals from said source crude oil.

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 1, wherein said source of said dry crude oil has an API index of between 7°

API and 20°

API.

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. The method as defined in claim 1, further including step of collecting and condensing vaporized water.

11. The method as defined in claim 1, further including a step of collecting and condensing light hydrocarbon fluid.

12. The method as defined in claim 10, further including the step of purifying said condensed water.

13. The method as defined in claim 10, 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. A method of removing water from a crude oil containing water, comprising of steps of:

a) providing a source of crude oil containing water;

b) 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 a temperature sufficient to vaporize water contacting said surface;

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

d) re-circulating said dry crude oil for contact immediately below said vaporizing surface; and

e) re-circulating said dry 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.

16. The method as defined in claim 15, wherein prior to step b), said source is pre-conditioned.

17. The method as defined in claim 16, wherein in preconditioning includes removal of solid and mineral from said source.

19. The method as defined in claim 16, further including the step of collecting gaseous vapors evolving from said dehydrator.

20. The method as defined in claim 16, further including the step of collecting light hydrocarbon liquids formed during dehydration.

21. The method as defined in claim 16, wherein separated minerals are collected in a concentrated brine.

18. A method of removing water from crude oil containing water, comprising of steps of:

a) providing a source of crude oil containing water;

b) 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 a temperature sufficient to vaporize water contacting said surface;

c) pre-washing said source of crude oil containing water to remove alkali metals and alkaline earth metals;

d) separating said alkali metals and said alkaline earth metals and oil in a preliminary separation step;

e) passing washed oil into said dehydrator to flash evaporate water from said washed oil to remove water therefrom;

f) pre-heating crude oil to be treated in said dehydrator with treated dehydrated crude oil from said dehydrator to return heat energy lost from flash evaporating water;

g) re-circulating said dry crude oil for contact immediately below said vaporizing surface of said dry crude oil, whereby a uniform surface temperature of said vaporizing surface is maintained.