IP Library Granted Patent US 8,022,019
Granted Patent B2
US 8,022,019 · App. 12/622,900 · Granted Sep 20, 2011

Method of making proppant used in gas or oil extraction

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Quick Facts
Patent No.
US 8,022,019
App. No.
12/622,900
Granted
Sep 20, 2011
Kind
B2
Abstract

Method and system for making a spherical proppant having a selected grade from a naturally occurring mined mineral having a hardness of over 6.0 Mohs. The method and system involves preprocessing the mineral mechanically into a semi-dry feedstock comprising a mass of particles with initial sphericity values generally less than 0.60; subjecting the semi-dry feedstock to an aggressive abrasive attrition operation for a process time; and, controlling the process time to a value wherein the particles of the feedstock are converted to final processed particles having a sphericity greater than 0.60 by increasing the sphericity of the feedstock particles by at least 0.10. In addition, the processed particles are screened to obtain a proppant having a selected grade.

Claims (33)

1. A method of making a spherical proppant having a selected grade from a naturally occurring mined mineral having a hardness of over 6.0 Mohs, said method comprising:

(a) preprocessing said mineral mechanically into a semi-dry feedstock comprising a mass of particles with initial sphericity values generally less than 0.60;

(b) subjecting said feedstock to abrasive attrition for a process time; and,

(c) controlling said process time to a value wherein said particles of said feedstock are converted to processed particles having a sphericity greater than 0.60 by increasing the sphericity of said feedstock particles by at least 0.10.

2. The method of claim 1 further including:

(d) washing said processed particles to remove fines;

(e) drying said processed particles; and,

(f) screening said processed particles to obtain a proppant having said selected grade.

3. The method as defined in claim 2 wherein said controlled selected time is greater than about 12 hours.

4. The method as defined in claim 3 further including:

(g) measuring the sphericity of said process particles after a first controlled time; and,

(h) converting said first controlled time to the process time if said measured sphericity exceeds a given value.

5. The method as defined in claim 4 where said given value is in the range of 0.75 to 0.90.

6. The method as defined in claim 2 further including:

(g) controlling the preprocessing operation by the size of said selected grade.

7. The method as defined in claim 1 wherein said controlled selected time is greater than about 12 hours.

8. The method as defined in claim 7 further including:

(d) measuring the sphericity of said process particles after a first controlled time; and,

(e) converting said first controlled time to the process time if said measured sphericity exceeds a given value.

9. The method as defined in claim 8 where said given value is in the range of 0.75 to 0.90.

10. The method of claim 1 wherein said mineral is silica sand and said proppant is frac sand.

11. The method as defined in claim 10 wherein at least 99% of said processed particles have a sphericity in the range of 0.75 to 0.90.

12. The method as defined in claim 10 wherein said selected grade is a grade with a maximum value of 6 to 35 mesh and a minimum value of 30-140 mesh.

13. A method as defined in claim 10 wherein said silica sand has a SiO 2 content of at least 80% and a general particle shape classified as between round and angular and a particle size of less than about 8.0 mm.

14. A method as defined in claim 10 wherein said preprocessed feedstock has a particle size coarser than about 350 mesh.

15. The method as defined in claim 1 wherein said feedstock is combined with water before being subjected to abrasive attrition.

16. The method as defined in claim 15 wherein said water is in the range of 5-20 percent by weight of said feedstock and water.

17. The method as defined in claim 1 wherein at least 99% of said processed particles have a sphericity in the range of 0.75 to 0.90.

18. The method as defined in claim 1 wherein said selected grade is a grade with a maximum value of 6 to 35 mesh and a minimum value of 30-140 mesh.

19. A method as defined in claim 1 wherein said preprocessed feedstock has a particle size coarser than about 350 mesh.

20. The method as defined in claim 1 wherein said semi-dry feedstock has at least 5 percent moisture content.

21. The method as defined in claim 1 wherein said semi-dry feedstock has less than 20 percent moisture content.

22. The method as defined in claim 1 further including conversion of said process from batch to continuous before said feedstock is washed.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded Jan 1, 2021
From: WILMINGTON SAVINGS FUND SOCIETY, FSB
To: COVIA HOLDINGS LLC (FORMERLY COVIA HOLDINGS CORPORATION)
Reel/Frame 054886/0318 →
SECURITY INTEREST Recorded Oct 19, 2020
From: BARCLAYS BANK PLC
To: WILMINGTON SAVINGS FUND SOCIETY, FSB
Reel/Frame 054113/0352 →
SECURITY INTEREST Recorded Aug 27, 2018
From: COVIA HOLDINGS CORPORATION; FAIMOUNT SANTROL INC.; TECHNISAND, INC.; SELF-SUSPENDING PROPPANT LLC
To: BARCLAYS BANK PLC, AS COLLATERAL AGENT
Reel/Frame 047320/0483 →
CHANGE OF NAME Recorded Aug 9, 2018
From: UNIMIN CORPORATION
To: COVIA HOLDINGS CORPORATION
Reel/Frame 046757/0764 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 20, 2009
From: RUSH, DAVID JOHN; GONZALEZ, JUAN LEAL
To: UNIMIN CORPORATION
Reel/Frame 023551/0144 →