Far-field diversion with pulsed proppant in subterranean fracturing operations
US-2017009129-A1 · Jan 12, 2017 · US
US11732179B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11732179-B2 |
| Application number | US-201916982154-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 3, 2019 |
| Priority date | Apr 3, 2018 |
| Publication date | Aug 22, 2023 |
| Grant date | Aug 22, 2023 |
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Methods include pumping a fracturing pad fluid into a subterranean formation under conditions of sufficient rate and pressure to create at least one fracture in the subterranean formation, the fracturing pad fluid including a carrier fluid and a plurality of bridging particles, the bridging particles forming a bridge in a fracture tip of a far field region of the formation. Methods further include pumping a first plurality of fibers into the subterranean formation to form a low permeability plug with the bridging particles, and pumping a proppant fluid comprising a plurality of proppant particles.
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What is claimed: 1. A method, comprising: pumping a first stage consisting essentially of a fracturing pad fluid into a subterranean formation under conditions of sufficient rate and pressure to create at least one fracture in the subterranean formation, the fracturing pad fluid consisting essentially of a carrier fluid and a plurality of bridging particles, the plurality of bridging particles forming a bridge in a fracture tip within a far field region of the formation; then, pumping a second stage comprising a fluid consisting essentially of a first plurality of fibers into the subterranean formation to form a plug with the plurality of bridging particles directly after pumping the first stage; and then, pumping a third stage comprising a proppant fluid consisting essentially of a plurality of proppant particles after pumping the second stage. 2. The method of claim 1 , wherein the plurality of bridging particles have a diameter ranging from 0.1 to 10 mm. 3. The method of claim 2 , wherein the plurality of bridging particles have a monomodal or a multimodal distribution. 4. The method of claim 1 , wherein the first plurality of fibers comprises a first quantity of the first plurality of fibers, and wherein the fracturing pad fluid further consists essentially of a second quantity of the first plurality of fibers such that the second quantity of the first plurality of fibers are intermingled with the plurality of bridging particles to form the bridge after pumping the fracturing pad fluid into subterranean formation. 5. The method of claim 1 , wherein the first plurality of fibers are pumped sequentially via the fluid after the plurality of bridging particles in the fracturing pad fluid such that the first plurality of fibers form a deposit on the bridge. 6. The method of claim 5 , wherein the fracturing pad fluid further consists essentially of a second plurality of fibers such that the second plurality of fibers are intermingled with the plurality of bridging particles to form the bridge on which the first plurality of fibers are deposited. 7. The method of claim 6 , wherein the second plurality of fibers is added in a concentration of 0.1-600 ppt (pounds per thousand gallons). 8. The method of claim 1 , wherein the first plurality of fibers are selected from the group of cellulose and cellulose derivatives fibers. 9. The method of claim 1 , wherein the first plurality of fibers are selected from the group of organic polymers. 10. The method of claim 1 , wherein the first plurality of fibers have an aspect ratio of 1.5 to 1000 and a length ranging from 0.05 mm to 30 mm. 11. The method of claim 1 , wherein the fracturing pad fluid has a viscosity of at least 4 cP at 511 s-1. 12. The method of claim 1 , wherein the plurality of bridging particles and the first plurality of fibers are introduced in the subterranean formation in such a manner to control a height and/or a length of the at least one fracture formed in the subterranean formation. 13. The method of claim 1 , wherein the plurality of bridging particles have respective particle sizes equal to or greater than respective particle sizes of the plurality of proppant particles. 14. The method of claim 1 , wherein the plurality of bridging particles and the plurality of proppant particles are selected from the group of sand and ceramic proppants. 15. A method, comprising: pumping a first stage consisting essentially of a plugging slurry non-uniformly into a far field region of a treatment zone of a subterranean formation, the plugging slurry consisting essentially of: a carrier fluid; and a plurality of bridging particles having a particle size sufficient to control a geometry of at least a fracture in a far field region, the plurality of bridging particles forming a bridge in a fracture tip within the far field region; pumping a second stage comprising a fluid consisting essentially of a first plurality of fibers into the far field region to form a plug with the plurality of bridging particles directly after pumping the first stage; pumping a third stage comprising a proppant fluid into the far field region of the treatment zone of the subterranean formation after pumping the second stage, wherein the proppant fluid consists essentially of a plurality of proppant particles; and continuing pumping the proppant fluid into the far field region until a fracture network forms. 16. The method of claim 15 , wherein the plurality of bridging particles have a diameter ranging from 0.1 to 10 mm. 17. The method of claim 15 , wherein the plurality of bridging particles have a monomodal or a multimodal distribution. 18. The method of claim 15 , wherein the first plurality of fibers comprises a first quantity of the first plurality of fibers, and wherein the plugging slurry further consists essentially of a second quantity of the first plurality of fibers such that the second quantity of the first plurality of fibers are intermingled with the plurality of bridging particles to form the bridge after pumping the plugging slurry. 19. The method of claim 15 , wherein the first plurality of fibers are pumped sequentially via the fluid after the plurality of bridging particles in the plugging slurry such that the first plurality of fibers form a deposit on the bridge. 20. The method of claim 19 , wherein the plugging slurry further consists essentially of a second plurality of fibers such that the second plurality of fibers are intermingled with the plurality of bridging particles to form the bridge on which the first plurality of fibers are deposited. 21. The method of claim 20 , wherein the second plurality of fibers is added in a concentration of 0.1-600 ppt. 22. The method of claim 20 , wherein the first and the second plurality of fibers are selected from the group of cellulose and cellulose derivatives fibers. 23. The method of claim 20 , wherein the first and the second plurality of fibers have an aspect ratio of 1.5 to 1000 and a length ranging from 0.05 mm to 30 mm. 24. The method of claim 20 , wherein an amount of the first and the second plurality of fibers ranges from 100 to 10000 lbs. 25. The method of claim 15 , wherein the plugging slurry has a viscosity of at least 4 cP at 511 s-1. 26. The method of claim 15 , wherein the plurality of bridging particles have respective particle sizes equal to or greater than respective particle sizes of the plurality of proppant particles. 27. The method of claim 15 , further comprising pumping a diversion fluid, wherein the diversion fluid is pumped during the second stage. 28. The method of claim 15 , wherein the plurality of bridging particles and the proppant particles are selected from the group of sand and ceramic proppants.
characterised by their form or by the form of their components, e.g. encapsulated material · CPC title
macromolecular compounds {(C09K8/512 takes precedence)} · CPC title
containing inorganic compounds · CPC title
of natural origin, e.g. polysaccharides, cellulose (C09K8/512 takes precedence) · CPC title
Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open · CPC title
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