Direct slurry weight sensor for well operation mixing process

US9695670B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9695670-B2
Application numberUS-201414212672-A
CountryUS
Kind codeB2
Filing dateMar 14, 2014
Priority dateMar 15, 2013
Publication dateJul 4, 2017
Grant dateJul 4, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

A slurry mixing system calculates a density of a slurry using measured pressure differential and based on a bulk velocity of the slurry. Slurry from mixing of dry blend and mix fluid enters a one or more tanks having agitators. A pump then pumps the slurry from the tank(s) to the well, and a portion of the slurry is recirculating back to a mixer. From the recirculated path, a direct slurry weight sensor measures a pressure differential of the slurry between two vertical measurement points of a known volume. The sensor can measure a velocity of the recirculated slurry, or the recirculated slurry can be maintained at a velocity. Based on these measures, the controller calculates a density of the slurry, monitors a ratio of the dry blend and the mix fluid, and adjusts the ratio based on the calculated density of the slurry if there is a discrepancy.

First claim

Opening claim text (preview).

What is claimed is: 1. A slurry mixing system of a well operation, comprising: a mixer mixing a dry blend and a mix fluid into a slurry; a first pump disposed downstream of the mixer, flow equipment delivering a first portion of the slurry from the first pump for the well operation, circulating a second portion of the slurry from the first pump back to the mixer for mixing, and circulating a third portion of the slurry from the first pump for sensing; a slurry sensor disposed in fluid communication with the third portion of the slurry, the slurry sensor measuring a pressure differential of the slurry between at least two vertical measurement points of a known volume, the flow equipment circulating the third portion of the slurry to a point downstream of the mixer and upstream of the first pump; and a controller operatively coupled to the slurry sensor, the controller obtaining the measured pressure differential and obtaining a velocity of the third portion of the slurry, the controller calculating a density of the slurry therefrom. 2. The system of claim 1 , further comprising the dry blend and the mix fluid as part of the system, wherein the dry blend comprises a cement or a fracking material, and wherein the mix fluid comprises water. 3. The system of claim 1 , wherein the mixer comprises at least one jet supplying the mix fluid to the dry blend. 4. The system of claim 1 , wherein the controller monitors a ratio of the dry blend and the mix fluid delivered to the mixer and adjusts the ratio based on the calculated density of the slurry. 5. The system of claim 1 , further comprising: a dry blend sensor operatively coupled to the controller and measuring the dry blend delivered to the mixer; and a fluid sensor operatively coupled to the controller and measuring the mix fluid delivered to the mixer. 6. The system of claim 1 , comprising at least one tank downstream of the mixer and upstream of the first pump, the at least one tank having at least one agitator agitating the slurry. 7. The system of claim 6 , wherein the at least one tank comprises: a first tank agitating the mixing of the slurry from the mixer; and a second tank averaging the slurry from the first tank. 8. The system of claim 1 , wherein the flow equipment comprises a second pump maintaining the velocity of the third portion of the slurry constant passing through the slurry sensor. 9. The system of claim 8 , comprising at least one tank disposed at the point downstream of the mixer and upstream of the first pump; and wherein the second pump discharges the third portion of the slurry to the at least one tank. 10. The system of claim 1 , wherein the slurry sensor comprises a conduit arranged vertically and having the known volume between first and second vertical locations as the at least two vertical measurement points. 11. The system of claim 10 , wherein the slurry sensor comprises first and second pressure sensors sensing first and second pressures for the pressure differential respectively at the first and second vertical locations of the known volume. 12. The system of claim 11 , wherein the first and second pressure sensors each comprise: a sensing element for sensing pressure; a diaphragm disposed at the vertical location and in communication with the known volume; and a capillary communicating the sensing element with the diaphragm. 13. The system of claim 1 , wherein the slurry sensor comprises a velocity sensor sensing the velocity of the recirculated slurry. 14. The system of claim 1 , wherein the slurry sensor comprise a speed of sound sensor measuring a speed of sound in the slurry; and wherein the controller determines volumetric phase fractions for each phase in the slurry based on the pressure differential, the velocity, and the speed of sound in the slurry. 15. A slurry mixing method of a well operation, comprising: mixing a dry blend and a mix fluid into a slurry with a mixer; pumping the slurry with a first pump disposed downstream of the mixer; delivering, with flow equipment, a first portion of the slurry from the first pump for the well operation; circulating, with the flow equipment, a second portion of the slurry from the first pump back to the mixer for mixing and a third portion of the slurry from the first pump for sensing; measuring, with a slurry sensor disposed in fluid communication with the third portion of the slurry, a pressure differential of the slurry between at least two verticals measurements points of a known volume; circulating, with the flow equipment, the third portion of the slurry to a point downstream of the mixer and upstream of the first pump obtaining a velocity of the third portion of the slurry; and calculating a slurry density from the measured pressure differential and the obtained velocity. 16. The method of claim 15 , wherein the dry blend comprises a cement or a fracking material, and wherein the mix fluid comprises water. 17. The method of claim 15 , further comprising: monitoring a ratio of the dry blend and the mix fluid; and adjusting the ratio based on the calculated slurry density. 18. The method of claim 15 , further comprising maintaining the velocity of the third portion of the slurry constant passing through the known volume by pumping the third portion of the slurry with a second pump. 19. The method of claim 15 , wherein measuring the pressure differential comprises sensing first and second pressures for the pressure differential respectively at first and second vertical locations as the at least two measurement points of the known volume. 20. The method of claim 15 , wherein obtaining the velocity of the third portion of the slurry comprise measuring the velocity with a velocity sensor. 21. The method of claim 15 , further comprising: measuring a speed of sound in the third portion of the slurry; and determining volumetric phase fractions for each phase in the third portion of the slurry based on the pressure differential, the velocity, and the speed of sound in the recirculated slurry. 22. The method of claim 15 , wherein circulating, with the flow equipment, the second portion of the slurry from the first pump back to the mixer for remixing comprises circulating the second portion of the slurry to at least one jet mixing the dry blend and the mix fluid. 23. The method of claim 15 , wherein recirculating the third portion of the slurry to the point downstream of the mixer and upstream of the first pump comprises recirculating the third portion of the slurry to at least one tank disposed at the point downstream of the mixer and upstream of the first pump. 24. The system of claim 1 , wherein the flow equipment comprises: first piping in communication between the first pump and the mixer and delivering the second portion of the slurry; and second piping in communication between the first pump and the slurry sensor and delivering the third portion of the slurry. 25. The system of claim 24 , wherein the flow equipment comprises a second pump in communication with the second piping and maintaining the velocity of the third portion of the slurry constant passing through the slurry sensor. 26. The system of claim 24 , comprising at least one tank disposed at the point downstream of the mixer and upstream of the first pump, the second piping delivering the third portion of the slurry to the at least one tank. 27. The s

Assignees

Inventors

Classifications

  • G05D21/02Primary

    characterised by the use of electric means · CPC title

  • E21B33/13Primary

    Methods or devices for cementing, for plugging holes, crevices or the like · CPC title

  • Operations & Transport · mapped topic

  • Operations & Transport · mapped topic

  • Operations & Transport · mapped topic

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What does patent US9695670B2 cover?
A slurry mixing system calculates a density of a slurry using measured pressure differential and based on a bulk velocity of the slurry. Slurry from mixing of dry blend and mix fluid enters a one or more tanks having agitators. A pump then pumps the slurry from the tank(s) to the well, and a portion of the slurry is recirculating back to a mixer. From the recirculated path, a direct slurry weig…
Who is the assignee on this patent?
Weatherford Lamb Inc, Weatherford Tech Holdings Llc
What technology area does this patent fall under?
Primary CPC classification G05D21/02. Mapped technology areas include Physics.
When was this patent published?
Publication date Tue Jul 04 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).