Hydraulic fracturing composition, method for making and use of same
US-2015096751-A1 · Apr 9, 2015 · US
US2017190957A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017190957-A1 |
| Application number | US-201715398120-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 4, 2017 |
| Priority date | Jan 5, 2016 |
| Publication date | Jul 6, 2017 |
| Grant date | — |
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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.
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.
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