Use of micro-particle amorphous silicate in well stimulation
View Patent ↗A treatment additive for hydraulic fracturing made of heated silica to create amorphous silicate with a Mohs hardness between 4.5 and 6 and a particles distribution with maximum diameter between 5 and 2600 microns that has been heated and shaped into amorphous shapes with large surface area to weight ratio and ultra-low settling velocity used to prop microfractures distal from well bore, especially in low viscosity and high temperature wells. The microparticle size and shape allow the treatment to effectively hold microfractures open, stimulate backpressure, and prevent leakoff; which has the added benefit of improving primary fracture development; refrac and frac protect productivity; and reduces the likelihood of interference between offset wells. An additional benefit is that the treatment doesn't contain crystalline silica.
1. A micro-particle silicate material for hydraulic fracturing treatments comprising:
silicate that has been heated to at least 1,700 degrees Celsius to become a liquid, cooled, and shattered into amorphous particles that contain more slivers, flat squares, small plane shapes, and irregular shapes than round shapes; and
wherein at least 51% of the particles have maximum diameters between 100 and 850 microns.
2. A micro-particle silicate material for hydraulic fracturing treatments comprising:
silicate that has been heated to at least 1,700 degrees Celsius to become a liquid, cooled, and shattered into amorphous particles that contain more slivers, flat squares, small plane shapes, and irregular shapes than round shapes; and
wherein at least 75% of the particles have maximum diameters between 40 and 1,000 microns.
3. A micro-particle silicate material for hydraulic fracturing treatments comprising:
silicate that has been heated to at least 1,700 degrees Celsius to become a liquid, cooled, and shattered into amorphous particles that contain more slivers, flat squares, small plane shapes, and irregular shapes than round shapes; and
wherein at least 97% of the particles have maximum diameters between 5 and 2600 microns.
4. The material of claim 3 , wherein less than 9% of a particle size distribution is larger than 150 microns in maximum diameter, 39% or more of said particle size distribution is below 50 microns in maximum diameter, and at least 17% of said particle size distribution is smaller than 5 microns in maximum diameter.
5. The material of claim 3 , wherein less than 20% of a particle size distribution is larger than 150 microns in maximum diameter, 20% or more of said particle size distribution is below 50 microns in maximum diameter, and at least 5% of said particle size distribution is smaller than 5 microns in maximum diameter.
6. The material of claim 3 , wherein less than 30% of a particle size distribution is larger than 150 microns in maximum diameter, 5% or more of said particle size distribution is below 50 microns in maximum diameter, and at least 1% of said particle size distribution is smaller than 20 microns in maximum diameter.
7. The material of claim 3 , wherein said amorphous silicate particles material comprises a Moh's hardness of between 4.5 and 6.
8. The material of claim 3 , wherein said amorphous silicate particles reduce in size during a hydraulic fracturing treatment.
9. The material of claim 8 , wherein said amorphous silicate particles reduce in size after 5,000 psi of pressure is applied.
10. The material of claim 9 , wherein a proportion of said amorphous silicate particles smaller than 100 microns in maximum diameter increase from below 60% to above 94% of total particles and particles smaller than 50 microns in maximum diameter increase from below 18% to above 49% of total particles after exposer exposure to 5,000 psi of pressure.
11. The material of claim 3 , wherein said material does not contain detectable amounts of crystalline silica.
12. A method of producing a micro-particle amorphous silicate material for hydraulic fracturing comprising:
selecting aggregate silicate with a Moh's hardness of between 4.5 and 6.0;
heating said aggregate silicate above 1700 degrees Celsius to become a liquid;
cooling said aggregate silicate below 1700 degrees Celsius;
shattering said aggregate silicate into amorphous particles that contain more slivers, flat squares, small plane shapes, and irregular shapes than round shapes; and
screening said particles to the desired sizes.
13. The method of claim 12 , wherein said particles are screened until at least 97% of said particles have a maximum diameter between 5 and 2,600 microns.
14. The method of claim 12 , wherein said particles are screened until at least 51% of said particles have a maximum diameter between 40 and 1,000 microns.
15. The method of claim 12 , wherein said particles are screened until at least 75% of said particles have a maximum diameter between 100 and 850 microns.
16. The method of claim 12 , further comprising, screening or mixing said particles until less than 9% of a particle size distribution is larger than 150 microns in maximum diameter; 39% or more of said particle size distribution is below 50 microns maximum diameter; and at least 17% of said particle size distribution is smaller than 5 microns in maximum diameter.
17. The method of claim 12 , further comprising, screening said particles until less than 20% of a particle size distribution is larger than 150 microns in maximum diameter, 20% or more of said particle size distribution is below 50 microns in maximum diameter, and at least 5% of said particle size distribution is smaller than 5 microns in maximum diameter.
18. The method of claim 12 , further comprising, screening or mixing said particles until less than 30% of a particle size distribution is larger than 150 microns in maximum diameter, 5% or more of said particle size distribution is below 50 microns in maximum diameter, and at least 1% of said particle size distribution is smaller than 20 microns in maximum diameter.