Compositions and methods of improving hydraulic fracture network

Patent metadata

Field	Value
Publication number	US-2016177693-A1
Application number	US-201514971139-A
Country	US
Kind code	A1
Filing date	Dec 16, 2015
Priority date	Dec 17, 2014
Publication date	Jun 23, 2016
Grant date	—

Abstract

A diverter fluid includes an aqueous carrier fluid, and a plurality of water-swellable polymer particles having a size of 0.01 to 100,000 micrometers. A method of hydraulically fracturing a subterranean formation penetrated by a reservoir includes injecting a fracturing fluid into the formation at a pressure sufficient to create or enlarge a fracture, injecting a diverter fluid into the formation, and injecting a fracturing fluid into the formation, wherein the flow of the fracturing fluid is impeded by the diverting agent and a surface fracture area of the fracture is increased. A method of controlling the downhole placement of a diverting agent is also disclosed, including injecting a diverter fluid including the diverting agent and an aqueous carrier fluid selected so that the polymer particles are fully swelled after contacting the aqueous carrier fluid for an amount of time sufficient to achieve a desired downhole placement.

First claim

1 . A diverter fluid, comprising
an aqueous carrier fluid; and a plurality of water-swellable polymer particles having a size of 0.01 to 100,000 micrometers.

2 . The diverter fluid of claim 1 , wherein the polymer particles are swellable to an average diameter of 1.1 to 1000 times greater than that of the same polymer particles that have not been swelled.

3 . The diverter fluid of claim 1 , wherein the polymer particles are fully swelled after contacting the aqueous diverter carrier fluid for 5 to 60 minutes.

4 . The diverter fluid of claim 1 , wherein the polymer particles are fully swelled after contacting the aqueous diverter carrier fluid for 1 to 36 hours.

5 . The diverter fluid of claim 1 , wherein the polymer particles are present in the diverter fluid in a concentration of 0.1 to 200 pounds per thousand gallons.

6 . The diverter fluid of claim 1 , wherein the polymer particles comprise a polysaccharide, poly(hydroxyC 1-8 alkyl (meth)acrylate)s such as poly(2-hydroxyethyl acrylate), poly(C 1-8 alkyl (meth)acrylate)s, poly((meth)acrylamide)s, poly(vinyl pyrrolidine), poly(vinyl acetate), or a combination comprising at least one of the foregoing.

7 . The diverter fluid of claim 1 , wherein the diverter carrier fluid comprises fresh water, brine, aqueous acid, aqueous base, or a combination comprising at least one of the foregoing.

8 . The diverter fluid of claim 1 , wherein the diverter fluid further comprises one or more of:
a lightweight particulate different from the water-swellable polymer particles, wherein the lightweight particulate has an apparent specific gravity of less than or equal to 3.25; an oxidative breaker; and an additional diverter different from the water-swellable polymer particles, preferably phthalic anhydride, polylactic acid, phthalic acid, rock salt, benzoic acid flakes, ground-up dissolvable ballsealers comprising collagen, ester-containing compounds, sodium chloride grains, polyglycolic acid, and combinations comprising at least one of the foregoing.

9 . A method of controlling the downhole placement of a diverting agent in a subterranean formation, the method comprising,
injecting into the formation the diverter fluid of claim 1 , wherein the aqueous carrier fluid is selected so that the polymer particles are fully swelled after contacting the aqueous carrier fluid for an amount of time sufficient to achieve a desired downhole placement.

10 . The method of claim 9 ,
wherein the carrier fluid is a low viscosity fluid comprising slickwater, freshwater, brine, aqueous acid, aqueous base, or a combination comprising at least one of the foregoing; wherein the polymer particles are fully swelled after contacting the aqueous carrier fluid for 5 to 60 minutes; and wherein the desired downhole placement is near wellbore.

11 . The method of claim 9 ,
wherein the carrier fluid is a high viscosity fluid comprising a gelled fluid or a foam; wherein the polymer particles are fully swelled after contacting the aqueous carrier fluid for 1 to 36 hours; and wherein the desired downhole placement is far field from a wellbore.

12 . The method of claim 9 , wherein the aqueous carrier fluid has a pH of 0 to 14 and the polymer particles are fully swelled after contacting the aqueous carrier fluid for 5 minutes to 36 hours.

13 . A method of hydraulically fracturing a subterranean formation penetrated by a reservoir or a well, the method comprising
injecting a fracturing fluid into the formation at a pressure sufficient to create or enlarge a fracture; injecting the diverter fluid of claim 1 into the formation; and injecting a fracturing fluid into the formation, wherein the flow of the fracturing fluid is impeded by the diverting agent and a surface fracture area of the fracture is increased.

14 . The method of claim 13 , wherein a desired downhole placement of the diverting agent in the subterranean formation is achieved by the method of claim 9 .

15 . The method of claim 13 , further comprising
monitoring an operational parameter, wherein the operational parameter is the injection rate of the fluid, the density of the fluid, the bottomhole treating pressure of the well, or the surface pressure at or near the surface of the well; and comparing the operational parameter after injecting of the diverter fluid into the formation with a pre-determined value for the operational parameter.

16 . The method of claim 13 , further comprising altering a stress in the well to increase the surface area of the fracture, wherein altering is by varying an injection rate of the fracturing fluid, varying the bottomhole pressure of the well, varying the density of the fracturing fluid, or a combination comprising at least one of the foregoing.

17 . The method of claim 13 , wherein
injecting the fracturing fluid into the formation is at a first pressure; a flow of the diverter fluid proceeds from a highly conductive zone to a less conductive zone; and injecting into the formation additional fracturing fluid is at a second pressure, wherein the second pressure is greater than the first pressure to increase a surface area of the fracture to a second surface area, wherein the second fracture area is greater than a fracture area created from a substantially similar method without employing the injecting into the formation the flow of the diverter fluid.

18 . The method of claim 13 , wherein the subterranean formation is a hydrocarbon-bearing formation.

19 . The method of claim 13 , wherein the subterranean formation is shale.

20 . The method of claim 13 , wherein each of the steps of the methods are continuous.

Assignees

• Gomaa Ahmed M
• Qu Qi
• Sun Hong
• Nelson Scott G
• Baker Hughes Inc

Inventors

• Gomaa Ahmed M
• Qu Qi
• Sun Hong
• Nelson Scott G

Classifications

• C09K8/70 Primary

  characterised by their form or by the form of their components, e.g. foams · CPC title

• C09K8/68

  containing organic compounds · CPC title

• C09K8/882

  obtained by reactions only involving carbon-to-carbon unsaturated bonds · CPC title

• E21B43/26 Primary

  by forming crevices or fractures · CPC title

• C09K8/90

  of natural origin, e.g. polysaccharides, cellulose · CPC title