Process for removing water from a water-containing crude oil

• US 6,042,718 A
• Filed: 11/25/1997
• Issued: 03/28/2000
• Est. Priority Date: 11/29/1996
• Status: Expired due to Fees

• Current Assignee: Foremost Universal LP
• Original Assignee: Universal Industries Corp.
• Inventors: Brauer, Edward E., Bland, Linden H.
• Primary Examiner(s): Griffin, Walter D.
• Assistant Examiner(s): Nguyen, Tam M.
• Application Number:
  US08/977,872
• Time in Patent Office: 854 Days
• Field of Search: 208/187, 203/14
• US Class Current: 208/187
• CPC Class Codes: C10G 31/06 by heating, cooling, or pressure treatment
• CPC Class Codes: C10G 31/08 by treating with water
• CPC Class Codes: C10G 33/08 Controlling or regulating

Abstract

A process and apparatus for treating a crude oil containing water. An inlet introduces a flow of the crude oil into the apparatus, wherein at least a portion of the water is a vapor. A first separator disrupts the crude oil flow in order to separate at least a portion of the vapor from the crude oil to produce a treated oil. A heater heats the treated oil to produce a heated treated oil. Means for recycling a first amount of the heated treated oil from the heater to the inlet are provided. The first amount is at least sufficient to heat the crude oil to a temperature such that at least a portion of the water forms the vapor. At least one oil outlet removes the treated oil and at least one vapor outlet removes the vapor. Finally, means are provided for producing the flow of the crude oil. The process is preferably conducted using the apparatus.

Claims

1. A process for treating a flow of crude oil containing water through an apparatus having an inlet, the process comprising the steps of:

(a) introducing the flow of the crude oil into the apparatus at the inlet, wherein at least a portion of the water contained in the crude oil is a vapour;

(b) first disrupting the flow of the crude oil in order to separate at least a portion of the vapour from the crude oil to produce a treated oil;

(c) heating the treated oil to produce a heated treated oil; and

(d) recycling a first amount of the heated treated oil to the inlet for mixing with the crude oil, wherein the first amount of the heated treated oil is at least sufficient to heat the crude oil to a temperature such that at least a portion of the water contained in the crude oil forms the vapour.

2. The process as claimed in claim 1 further comprising the step of second disrupting the flow of the heated treated oil, prior to the recycling step, in order to separate at least a further portion of the vapor from the heated treated oil.

3. The process as claimed in claim 2 wherein the heating step is comprised of heating the treated oil to a temperature such that upon the mixing of the first amount of the heated treated oil with the crude oil at the inlet, at least a portion of the water contained in the crude oil forms the vapor.

4. The process as claimed in claim 3 wherein substantially all of the water contained in the crude oil forms the vapour.

5. The process as claimed in claim 4 wherein the heating step is comprised of heating the treated oil to a temperature of greater than or equal to the boiling point of the water in the crude oil.

6. The process as claimed in claim 5 wherein the heating step is comprised of heating the treated oil to a temperature of between about 135 and 150 degrees Celsius.

7. The process as claimed in claim 5 further comprising the step of removing a second amount of the heated treated oil from the apparatus for further processing or storage.

8. The process as claimed in claim 7 further comprising the step of removing the vapour from the apparatus for further processing or storage.

9. The process as claimed in claim 5 wherein at least the heating step is conducted at a pressure below atmospheric pressure.

10. The process as claimed in claim 5 wherein at least the first disrupting step, the heating step and the second disrupting step are conducted at a pressure of about equal to or greater than atmospheric pressure.

11. The process as claimed in claim 10 wherein at least the first disrupting step, the heating step and the second disrupting step are conducted at a pressure of between about 2 and 5 psig.

12. The process as claimed in claim 5 wherein the first amount of the heated treated oil recycled by the recycling step is at least sufficient to heat the crude oil to a temperature of greater than or equal to about 105 degrees Celsius.

13. The process as claimed in claim 5 further comprising the step of inhibiting channeling and the formation of foam during the heating step.