Apparatus and method for oilfield material delivery
US-9133701-B2 · Sep 15, 2015 · US
US9694993B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9694993-B2 |
| Application number | US-201414539752-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 12, 2014 |
| Priority date | Nov 12, 2013 |
| Publication date | Jul 4, 2017 |
| Grant date | Jul 4, 2017 |
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A process for operating a settling slurry transportation pipeline is provided, comprising: determining the deposition velocity for a particular slurry being transported through the pipeline; and operating the pipeline at an operating velocity at or near the deposition velocity to form a stationary or near stationary bed of solids that will still allow the slurry to freely flow through the pipeline and not plug the pipeline.
Opening claim text (preview).
We claim: 1. A process for operating a slurry transportation pipeline designed for transporting a slurry derived from an oil sands extraction process, comprising: determining the deposition velocity for a particular slurry derived from an oil sands extraction process being transported through the pipeline; and operating the pipeline at an operating velocity below the deposition velocity to form a stationary or near stationary bed of solids at or near the 6 o'clock position of the pipeline that will still allow the slurry to freely flow through the pipeline and not plug the pipeline while reducing the pipeline wear rate. 2. The process as claimed in claim 1 , wherein the operating velocity is not more than about 40% below the deposition velocity. 3. The process as claimed in claim 1 , wherein the operating velocity is about 5% below the deposition velocity. 4. The process as claimed in claim 1 , wherein the operating velocity is at least about 10% below the deposition velocity. 5. The process as claimed in claim 1 , wherein the operating velocity is between about 10% to about 40% below the deposition velocity. 6. The process as claimed in claim 1 , wherein the slurry is an oil sand slurry comprising mined oil sand and water and the pipeline consists of 24″ pipe, whereby operating the pipeline at the operating velocity below the deposition velocity is accomplished by replacing some or all of the 24″ pipe of the pipeline with 28″ pipe while maintain the original hydraulics and pumping capacity. 7. The process as claimed in claim 1 , wherein operating the pipeline at the operating velocity below the deposition velocity is accomplished by installing adequate pump horsepower to lift or move the stationary bed when pipeline pressure gradients are trending upwards at constant flow rate and/or the pipeline capacity is being reduced at a given pump speed. 8. The process as claimed in claim 1 , wherein the relative height of the stationary or near stationary bed of solids is between about 0.05 and 0.1. 9. The process as claimed in claim 1 , wherein the relative height of the stationary or near stationary bed of solids is between about 0.05 and 0.2. 10. The process as claimed in claim 1 , wherein the relative height of the stationary or near stationary bed of solids is less than about 0.25 but greater than about 0.05. 11. The process as claimed in claim 1 , wherein the height of the stationary or near stationary bed is controlled by pressure gradient, densitometry, electrical tomography, ultrasonic velocity measurements or other instrumentation to avoid pipeline blockage by the stationary or near stationary bed. 12. The process as claimed in claim 1 , whereby the wear on the pipeline is reduced so as to increase the overall pipeline service life. 13. The process as claimed in claim 11 , whereby the height of the stationary or near stationary bed is about 5% of the diameter of the pipeline. 14. The process as claimed in claim 11 , whereby the height of the stationary or near stationary bed is between about 5% and about 20% of the diameter of the pipeline. 15. The process as claimed in claim 11 , whereby the height of the stationary or near stationary bed is less than about 25% of the diameter of the pipeline but greater than about 5% of the diameter of the pipeline.
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