Treatment fluids and methods of use in subterranean formations
Abstract
The present invention relates to subterranean treatment operations, and more particularly to improved bridging agents comprising a degradable material, improved subterranean treatment fluids comprising such improved bridging agents, and methods of using such improved subterranean treatment fluids in subterranean formations. An example of a method of the present invention is a method of drilling a well bore in a subterranean formation. Another example of a method of the present invention is a method of forming a self-degrading filter cake in a subterranean formation. Another example of a method of the present invention is a method of degrading a filter cake in a subterranean formation. An example of a composition of the present invention is a treatment fluid including a viscosifier, a fluid loss control additive, and a bridging agent comprising a degradable material. Another example of a composition of the present invention is a bridging agent comprising a degradable material.
Claims
exact text as granted — not AI-modified1 . A method of drilling a well bore in a subterranean formation, comprising the step of drilling a well bore in a subterranean formation using a treatment fluid comprising a base fluid, a viscosifier, a fluid loss control additive, and a bridging agent that comprises a degradable material.
2 . The method of claim 1 further comprising the step of permitting the bridging agent to form a filter cake in the well bore.
3 . The method of claim 2 wherein the step of permitting the bridging agent to form a filter cake in the well bore comprises forming the filter cake upon a surface in the formation.
4 . The method of claim 2 further comprising the step of permitting the filter cake to degrade.
5 . The method of claim 1 wherein the base fluid comprises an organic fluid.
6 . The method of claim 5 wherein the organic fluid comprises a mineral oil, a synthetic oil, or an ester.
7 . The method of claim 6 wherein the organic fluid is kerosene or diesel.
8 . The method of claim 1 wherein the base fluid is present in the treatment fluid in an amount sufficient to form a pumpable treatment fluid.
9 . The method of claim 8 wherein the base fluid is present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid.
10 . The method of claim 1 wherein the viscosifier comprises an organophilic clay, a synthetic oil-soluble polymer, or a polymeric fatty acid.
11 . The method of claim 10 wherein the viscosifier is an organophilic clay.
12 . The method of claim 1 wherein the viscosifier is present in the treatment fluid in an amount sufficient to provide a desired degree of solids suspension.
13 . The method of claim 1 wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds viscosifier per barrel of treatment fluid.
14 . The method of claim 1 wherein the fluid loss control additive comprises a synthetic oil-soluble polymer, a powdered hydrocarbon resin, or organophilic lignite.
15 . The method of claim 1 wherein the fluid loss control additive is a synthetic, oil-soluble polymer.
16 . The method of claim 1 wherein the fluid loss control additive is present in the treatment fluid in an amount sufficient to provide a desired degree of fluid loss control.
17 . The method of claim 1 wherein the fluid loss control additive is present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds of fluid loss control additive per barrel of treatment fluid.
18 . The method of claim 1 wherein the bridging agent is present in the treatment fluid in an amount sufficient to create an efficient filter cake.
19 . The method of claim 1 wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid.
20 . The method of claim 1 wherein the degradable material comprises a polysaccharide, a chitin, a chitosan, a protein, an orthoester, an aliphatic polyester, a poly(glycolide), a poly(lactide), a poly(ε-caprolactone), a poly(hydroxybutyrate), a polyanhydride, an aliphatic polycarbonate, a poly(orthoester), a poly(amino acid), a poly(ethylene oxide), or a polyphosphazene.
21 . The method of claim 1 wherein the degradable material further comprises a plasticizer or a stereoisomer of a poly(lactide).
22 . The method of claim 1 wherein the degradable material comprises poly(lactic acid).
23 . The method of claim 22 wherein the poly(lactic acid) is present in the degradable material in a stoichiometric amount.
24 . The method of claim 1 wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
25 . The method of claim 24 wherein the hydrated organic or inorganic compound comprises sodium acetate trihydrate, L-tartaric acid disodium salt dihydrate, sodium citrate dihydrate, sodium tetraborate decahydrate, sodium hydrogen phosphate heptahydrate, sodium phosphate dodecahydrate, amylose, a starch-based hydrophilic polymer, or a cellulose-based hydrophilic polymer.
26 . The method of claim 24 wherein the degradable aliphatic polyester is present in the degradable material in a stoichiometric amount.
27 . The method of claim 26 wherein the hydrated organic or inorganic compound is present in the degradable material in a stoichiometric amount.
28 . The method of claim 24 wherein the degradable aliphatic polyester is poly(lactic acid).
29 . The method of claim 24 wherein the degradable material further comprises calcium carbonate.
30 . The method of claim 4 wherein the bridging agent does not begin to degrade until at least about 12 hours after its placement in the subterranean formation.
31 . The method of claim 1 wherein the treatment fluid further comprises a weighting agent, a salt, an emulsifier, a filtration control agent, and a pH control agent.
32 . The method of claim 4 wherein the base fluid is an organic fluid, present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid; wherein the fluid loss control additive is a synthetic, oil-soluble polymer, present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds fluid loss control additive per barrel of treatment fluid; wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds per barrel of treatment fluid; wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid; and wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
33 . A method of forming a self-degrading filter cake in a subterranean formation, comprising the steps of:
placing a treatment fluid in a subterranean formation, the treatment fluid comprising a base fluid, a viscosifier, a fluid loss control additive, and a bridging agent that comprises a degradable material; and permitting the bridging agent to form a self-degrading filter cake upon a surface in the formation, whereby fluid loss to the formation through the self-degrading filter cake is reduced.
34 . The method of claim 33 wherein the step of permitting the bridging agent to form a filter cake in the well bore comprises forming the filter cake upon a surface in the formation itself.
35 . The method of claim 33 wherein the base fluid comprises an organic fluid.
36 . The method of claim 35 wherein the organic fluid comprises a mineral oil, a synthetic oil, or an ester.
37 . The method of claim 36 wherein the organic fluid is kerosene or diesel.
38 . The method of claim 33 wherein the base fluid is present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid.
39 . The method of claim 33 wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds viscosifier per barrel of treatment fluid.
40 . The method of claim 33 wherein the fluid loss control additive is present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds fluid loss control additive per barrel of treatment fluid.
41 . The method of claim 33 wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid.
42 . The method of claim 33 wherein the degradable material comprises poly(lactic acid).
43 . The method of claim 33 wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
44 . The method of claim 43 wherein the degradable aliphatic polyester is poly(lactic acid).
45 . The method of claim 33 wherein the base fluid is an organic fluid, present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid; wherein the fluid loss control additive is a synthetic, oil-soluble polymer, present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds fluid loss control additive per barrel of treatment fluid; wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds per barrel of treatment fluid; wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid; and wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
46 . A method of degrading a filter cake in a subterranean formation, the filter cake having been deposited therein by a treatment fluid comprising a bridging agent, comprising the steps of:
utilizing a bridging agent comprising a degradable material; and permitting the degradable material to degrade.
47 . The method of claim 46 wherein the treatment fluid further comprises a base fluid, a viscosifier, and a fluid loss control additive.
48 . The method of claim 47 wherein the base fluid comprises an organic fluid.
49 . The method of claim 48 wherein the organic fluid comprises a mineral oil, a synthetic oil, or an ester.
50 . The method of claim 49 wherein the organic fluid is kerosene or diesel.
51 . The method of claim 46 wherein the base fluid is present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid.
52 . The method of claim 47 wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds per barrel of treatment fluid.
53 . The method of claim 47 wherein the fluid loss control additive is present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds fluid loss control additive per barrel of treatment fluid.
54 . The method of claim 46 wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid.
55 . The method of claim 46 wherein the degradable material comprises poly(lactic acid).
56 . The method of claim 46 wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
57 . The method of claim 56 wherein the degradable aliphatic polyester is poly(lactic acid).
58 . The method of claim 47 wherein the base fluid is an organic fluid, present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid; wherein the fluid loss control additive is a synthetic, oil-soluble polymer, present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds fluid loss control additive per barrel of treatment fluid; wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds per barrel of treatment fluid; wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid; and wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
59 . A treatment fluid comprising a viscosifier, a fluid loss control additive, and a bridging agent comprising a degradable material.
60 . The treatment fluid of claim 59 further comprising a base fluid.
61 . The treatment fluid of claim 60 wherein the base fluid comprises an organic fluid.
62 . The treatment fluid of claim 61 wherein the organic fluid comprises a mineral oil, a synthetic oil, or an ester.
63 . The treatment fluid of claim 62 wherein the organic fluid is kerosene or diesel.
64 . The treatment fluid of claim 60 wherein the base fluid is present in an amount sufficient to form a pumpable treatment fluid.
65 . The treatment fluid of claim 64 wherein the base fluid is present in an amount in the range of from about 20% to about 99% by volume of the treatment fluid.
66 . The treatment fluid of claim 65 wherein the viscosifier comprises an organophilic clay, a synthetic, oil-soluble polymer, or a polymeric fatty acid.
67 . The treatment fluid of claim 66 wherein the viscosifier is an organophilic clay.
68 . The treatment fluid of claim 59 wherein the viscosifier is present in an amount sufficient to provide a desired degree of solids suspension.
69 . The treatment fluid of claim 68 wherein the viscosifier is present in an amount in the range of from about 1 to about 20 pounds viscosifier per barrel of treatment fluid.
70 . The treatment fluid of claim 59 wherein the fluid loss control additive comprises a synthetic, oil-soluble polymer, a powdered hydrocarbon resin, or organophilic lignite.
71 . The treatment fluid of claim 70 wherein the fluid loss control additive is a synthetic, oil-soluble polymer.
72 . The treatment fluid of claim 59 wherein the fluid loss control additive is present in an amount sufficient to provide a desired degree of fluid loss control.
73 . The treatment fluid of claim 71 wherein the fluid loss control additive is present in an amount in the range of from about 1 to about 30 pounds per barrel of treatment fluid.
74 . The treatment fluid of claim 59 wherein the bridging agent comprising the degradable material is present in an amount sufficient to create an efficient filter cake.
75 . The treatment fluid of claim 74 wherein the bridging agent is present in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid.
76 . The treatment fluid of claim 59 wherein the degradable material comprises a polysaccharide, a chitin, a chitosan, a protein, an orthoester, an aliphatic polyester, a poly(glycolide), a poly(lactide), a poly(ε-caprolactone), a poly(hydroxybutyrate), a polyanhydride, an aliphatic polycarbonate, a poly(orthoester), a poly(amino acid), a poly(ethylene oxide), or a polyphosphazene.
77 . The treatment fluid of claim 59 wherein the degradable material further comprises a plasticizer or a stereoisomer of a poly(lactide).
78 . The treatment fluid of claim 59 wherein the degradable material comprises
79 . The treatment fluid of claim 78 wherein the poly(lactic acid) is present in the degradable material in a stoichiometric amount.
80 . The treatment fluid of claim 59 wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
81 . The treatment fluid of claim 80 wherein the hydrated organic or inorganic compound comprises sodium acetate trihydrate, L-tartaric acid disodium salt dihydrate, sodium citrate dihydrate, sodium tetraborate decahydrate, sodium hydrogen phosphate heptahydrate, sodium phosphate dodecahydrate, amylose, a starch-based hydrophilic polymer, or a cellulose-based hydrophilic polymer.
82 . The treatment fluid of claim 80 wherein the degradable aliphatic polyester is present in the degradable material in a stoichiometric amount.
83 . The treatment fluid of claim 80 wherein the hydrated organic or inorganic compound is present in the degradable material in a stoichiometric amount.
84 . The treatment fluid of claim 80 wherein the degradable aliphatic polyester is poly(lactic acid).
85 . The treatment fluid of claim 80 wherein the degradable material further comprises calcium carbonate.
86 . The treatment fluid of claim 59 wherein the bridging agent does not begin to degrade until at least about 12 hours after it has been placed in a subterranean formation.
87 . The treatment fluid of claim 59 wherein the treatment fluid further comprises a weighting agent, a salt, an emulsifier, a filtration control agent, and a pH control agent.
88 . The treatment fluid of claim 59 wherein the base fluid is an organic fluid, present in the treatment fluid in an amount in the range of from about 20% to about 99% by volume of the treatment fluid; wherein the fluid loss control additive is an oil-soluble polymer, present in the treatment fluid in an amount in the range of from about 1 to about 30 pounds fluid loss control additive per barrel of treatment fluid; wherein the viscosifier is present in the treatment fluid in an amount in the range of from about 1 to about 20 pounds per barrel of treatment fluid; wherein the bridging agent is present in the treatment fluid in an amount in the range of from about 0.1% to about 32% by weight of the treatment fluid; and wherein the degradable material comprises a degradable aliphatic polyester and a hydrated organic or inorganic compound.
89 . A bridging agent comprising a degradable material.
90 . The bridging agent of claim 89 wherein the degradable material comprises a polysaccharide, a chitin, a chitosan, a protein, an orthoester, an aliphatic polyester, a poly(glycolide), a poly(lactide), a poly(ε-caprolactone), a poly(hydroxybutyrate), a polyanhydride, an aliphatic polycarbonate, a poly(orthoester), a poly(amino acid), a poly(ethylene oxide), or a polyphosphazene.
91 . The bridging agent of claim 89 wherein the degradable material comprises poly(lactic acid).Join the waitlist — get patent alerts
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