Hydraulic fracturing using super absorbent polymer having controlled particle size

US2017190957A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2017190957-A1
Application numberUS-201715398120-A
CountryUS
Kind codeA1
Filing dateJan 4, 2017
Priority dateJan 5, 2016
Publication dateJul 6, 2017
Grant date

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

A hydraulic fracturing process comprises combining an aqueous carrier with a superabsorbent polymer and a plurality of proppant particles to form a fracturing fluid; and disposing the fracturing fluid in a downhole environment. When the aqueous carrier has a total dissolved solid content of equal to or less than 400 parts per million and a hardness of less than 100 parts per million as calcium carbonate, the superabsorbent polymer comprises particles having a size of about 145 microns to about 600 microns. When the aqueous carrier has a total dissolved solid content of greater than 400 parts per million to less than 8,000 parts per million and a hardness of greater than 100 parts per million to less than 2,500 parts per million as calcium carbonate, the superabsorbent polymer comprises particles having a size of about 145 microns to about 300 microns.

First claim

Opening claim text (preview).

1 . A hydraulic fracturing process characterized by: combining an aqueous carrier with a superabsorbent polymer and a plurality of proppant particles to form a fracturing fluid; and disposing the fracturing fluid in a downhole environment, wherein one of the following conditions apply: (i) the aqueous carrier has a total dissolved solid content of equal to or less than 400 parts per million and a hardness of less than 100 parts per million as calcium carbonate, and the superabsorbent polymer comprises particles having a size of about 145 microns to about 600 microns; or (ii) the aqueous carrier has a total dissolved solid content of greater than 400 parts per million to less than 8,000 parts per million and a hardness of greater than 100 parts per million to less than 2,500 parts per million as calcium carbonate, and the superabsorbent polymer comprises particles having a size of about 145 microns to about 300 microns. 2 . The process of claim 1 , wherein the aqueous carrier has a total dissolved solid content of equal to or less than 400 parts per million and a hardness of less than 100 parts per million as calcium carbonate; and the superabsorbent polymer comprises particles having a size of about 145 microns to about 600 microns. 3 . The process of claim 2 , wherein the superabsorbent material comprises particles having a size of about 145 microns to about 425 microns. 4 . The process of claim 2 , wherein the superabsorbent polymer comprises a repeat unit derived from an acrylate, an acrylamide, a vinylpyrrolidone, a vinyl acetate, a vinyl alcohol, a saccharide, a 2-acrylamide-2-methylpropanesulfonic acid, a derivative thereof, or a combination thereof; and the superabsorbent polymer comprises a plurality of crosslinks. 5 . The process of claim 4 , wherein the crosslinks of the superabsorbent polymer are formed prior to combining the superabsorbent polymer with the aqueous carrier and the proppant particles. 6 . The process of claim 2 , wherein fracturing fluid comprises less than about 40 pounds of the superabsorbent polymer per one thousand gallons of the fracturing fluid. 7 . The process of claim 1 , wherein the fracturing fluid has a viscosity of greater than about 250 cps at 23° C. in about 3 to about 5 minutes after the aqueous carrier, the superabsorbent polymer, and the proppant particles are combined. 8 . The process of claim 1 , wherein the proppant particles have a size of about 200 microns to about 850 microns. 9 . The process of claim 1 , wherein greater than about 85 wt % of the superabsorbent polymer has a particle size of about 145 microns to about 600 microns, based on the total weight of the super absorbent polymer. 10 . The process of claim 1 , wherein the aqueous carrier has a total dissolved solid content of greater than 400 parts per million to less than 8,000 parts per million and a hardness of greater than 100 parts per million to less than 2,500 parts per million as calcium carbonate; and the superabsorbent polymer comprises particles having a size of about 145 microns to about 300 microns. 11 . The process of claim 10 , wherein the aqueous carrier has a total dissolved solid content of greater than 1,000 parts per million to less than 5,000 parts per million; and a hardness of greater than 250 parts per million to about 2,000 parts per million as calcium carbonate. 12 . The process of claim 10 , wherein the aqueous carrier has a total dissolved solid content of greater than 2,000 parts per million to less than 4,000 parts per million; and a hardness of greater than 500 parts per million to about 1,500 parts per million as calcium carbonate. 13 . The process of claim 10 , wherein the superabsorbent polymer comprises a repeat unit derived from an acrylate, an acrylamide, a vinylpyrrolidone, a vinyl acetate, a vinyl alcohol, a saccharide, a 2-acrylamide-2-methylpropanesulfonic acid, a derivative thereof, or a combination thereof; and the superabsorbent polymer comprises a plurality of crosslinks. 14 . The process of claim 13 , wherein the crosslinks of the superabsorbent polymer are formed prior to combining the superabsorbent polymer with the aqueous carrier and the proppant particles. 15 . The process of claim 10 , wherein fracturing fluid comprises less than about 60 pounds of the superabsorbent polymer per one thousand gallons of the fracturing fluid. 16 . The process of claim 10 , wherein greater than about 85 wt % of the super absorbent polymer has a size of about 145 microns to about 300 microns, based on the total weight of the super absorbent polymer. 17 . A method of improving the efficiency of a superabsorbent polymer to carry proppants in a fracturing fluid, the method characterized by: providing a superabsorbent polymer; and combining the superabsorbent polymer with an aqueous carrier and a plurality of proppant particles; wherein one of the following conditions apply: (i) greater than about 85 wt % of the superabsorbent polymer has a particle size of about 145 microns to about 600 microns based on the total weight of the superabsorbent polymer, and the aqueous carrier has a total dissolved solid content of equal to or less than 400 parts per million and a hardness of less than 100 parts per million as calcium carbonate; or (ii) greater than about 85 wt % of the superabsorbent polymer has a particle size of about 145 microns to about 300 microns, based on the total weight of the superabsorbent polymer, and the aqueous fluid has a total dissolved solid content of greater than 400 parts per million to less than 8,000 parts per million and a hardness of greater than 100 parts per million to less than 2,500 parts per million as calcium carbonate. 18 . The method of claim 17 , wherein the superabsorbent polymer comprises a repeat unit derived from an acrylate, an acrylamide, a vinylpyrrolidone, a vinyl acetate, a vinyl alcohol, a saccharide, a 2-acrylamide-2-methylpropanesulfonic acid, a derivative thereof, or a combination thereof; and the superabsorbent polymer comprises a plurality of crosslinks. 19 . A hydraulic fracturing fluid characterized by: an aqueous carrier; a superabsorbent polymer; and a plurality of proppant particles, wherein one of the following conditions apply: (i) the aqueous carrier has a total dissolved solid content of equal to or less than 400 parts per million and a hardness of less than 100 parts per million as calcium carbonate, and greater than about 85 wt % of the superabsorbent polymer has a particle size of about 145 microns to about 600 microns based on the total weight of the superabsorbent polymer; or (ii) the aqueous carrier has a total dissolved solid content of greater than 400 parts per million to less than 8,000 parts per million and a hardness of greater than 100 parts per million to less than 2,500 parts per million as calcium carbonate, and greater than about 85% of the superabsorbent polymer has a particle size of about 145 microns to about 300 microns based on the total weight of the superabsorbent polymer.

Assignees

Inventors

Classifications

  • C09K8/685Primary

    containing cross-linking agents · CPC title

  • Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open · CPC title

  • macromolecular compounds · CPC title

  • containing cross-linking agents · CPC title

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What does patent US2017190957A1 cover?
A hydraulic fracturing process comprises combining an aqueous carrier with a superabsorbent polymer and a plurality of proppant particles to form a fracturing fluid; and disposing the fracturing fluid in a downhole environment. When the aqueous carrier has a total dissolved solid content of equal to or less than 400 parts per million and a hardness of less than 100 parts per million as calcium …
Who is the assignee on this patent?
Sun Hong, Carman Paul S, Volk Alyssa Michelle, and 2 more
What technology area does this patent fall under?
Primary CPC classification C09K8/685. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Jul 06 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).