US2012305254A1PendingUtilityA1
Methods to improve stability of high solid content fluid
Est. expiryJun 6, 2031(~4.9 yrs left)· nominal 20-yr term from priority
C09K 8/68C09K 8/035C09K 8/50C09K 2208/30C09K 8/575
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Abstract
A method of treating a subterranean formation of a well bore comprises providing a treatment fluid comprising a carrier fluid, a particulate material, a surfactant and micelles, wherein micelles are stabilized by the surfactant and act as particles in the treatment fluid; and introducing the treatment fluid into the wellbore.
Claims
exact text as granted — not AI-modified1 . A method of treating a subterranean formation of a well bore, comprising:
a. providing a treatment fluid comprising a carrier fluid, a particulate material, a surfactant and micelles, wherein micelles are stabilized by the surfactant and act as particles in the treatment fluid; and b. introducing the treatment fluid into the wellbore.
2 . The method of claim 1 , wherein the particulate material is proppant.
3 . The method of claim 1 , wherein the treatment fluid further comprises a viscosifying agent.
4 . The method of claim 1 , wherein the treatment fluid further comprises a degradable material.
5 . The method of claim 4 , wherein the particulate material has a first average particle size and the degradable particulate material has a second average particle size, wherein the second average particle size is between three to twenty times smaller than the first average particle size.
6 . The method of claim 5 , wherein the second average particle size is between five to ten times smaller than the first average particle size.
7 . The method of claim 5 , wherein the degradable particulate material has further an amount of particulates having a third average particle size, wherein the third average particle size is between three to twenty times smaller than the second average particle size.
8 . A method of treating a subterranean formation of a well bore, comprising:
a. providing a treatment fluid comprising a carrier fluid, a particulate material, a surfactant and micelles having an average size below 1 micron, wherein micelles are stabilized by the surfactant and act as particles in the treatment fluid; and b. introducing the treatment fluid into the wellbore.
9 . The method of claim 8 , wherein the micelles have an average size in the range of 10 nanometers to 500 nanometers.
10 . The method of claim 9 , wherein the micelles have an average size in the range of 50 nanometers to 200 nanometers.
11 . The method of claim 9 , wherein the particulate material is proppant.
12 . The method of claim 9 , wherein the treatment fluid further comprises a viscosifying agent.
13 . The method of claim 9 , wherein the treatment fluid further comprises a degradable material.
14 . The method of claim 13 , wherein the particulate material has a first average particle size and the degradable particulate material has a second average particle size, wherein the second average particle size is between three to twenty times smaller than the first average particle size.
15 . The method of claim 14 , wherein the second average particle size is between five to ten times smaller than the first average particle size.
16 . The method of claim 14 , wherein the degradable particulate material has further an amount of particulates having a third average particle size, wherein the third average particle size is between three to twenty times smaller than the second average particle size.
17 . A method of fracturing a subterranean formation of a well bore, comprising:
a. providing a treatment fluid comprising a carrier fluid, a particulate material, a surfactant and micelles having an average size below 1 micron, wherein micelles are stabilized by the surfactant and act as particles in the treatment fluid; and b. introducing the treatment fluid into the wellbore to initiate or propagate a fracture.
18 . The method of claim 17 , wherein the micelles have an average size in the range of 10 nanometers to 500 nanometers.
19 . The method of claim 18 , wherein the micelles have an average size in the range of 50 nanometers to 200 nanometers.
20 . The method of claim 17 , wherein the particulate material is proppant.Cited by (0)
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