PROPPANT PARTICULATES FORMED FROM DELAYED COKE
A fracturing fluid including proppant particulates formed from delayed coke, as well as a method for utilizing such fracturing fluid, are provided herein. The fracturing fluid includes a carrier fluid, as well as proppant particulates composed of delayed coke material. The method includes introducing the fracturing fluid into a subterranean formation and (optionally) depositing at least a portion of the proppant particulates within one or more fractures in the subterranean formation.
1 . A fracturing fluid, comprising:
carrier fluid; and
proppant particulates composed of delayed coke material.
2 . The fracturing fluid of claim 1 , further comprising second proppant particulates composed of a material that is not the delayed coke material.
3 . The fracturing fluid of claim 1 , wherein the delayed coke material is provided by processing delayed coke granules using at least one grinding or milling technique.
4 . The fracturing fluid of claim 1 , wherein the proppant particulates have an apparent density in the range of 1 . 0 grams per cubic centimeter (g/cm 3 ) to 2.0 g/cm 3 .
5 . The fracturing fluid of claim 1 , wherein the delayed coke proppant particulates have one or more of: (a) a carbon content of 82 weight percent (wt %) to 90 w1%; (b) a weight ratio of carbon to hydrogen of 15:1 to 30:1; (c) a sulfur content of 2 wt % to 8 wt %; (d) a nitrogen content of 1 wt % to 2 wt %; and (c) a combined vanadium and nickel content of 100 parts per million (ppm) to 3,000 ppm.
6 . The fracturing fluid of claim 1 , wherein the proppant particulates have a Hardgrove Grindability Index (HGI) value of 40 to 130.
7 . The fracturing fluid of claim 1 , wherein the proppant particulates have a Krumbein roundness value and a Krumbein sphericity value of ≥0.6, and wherein the Krumbein roundness value and the Krumbein sphericity value vary based on a grinding or milling technique used to process the delayed coke material.
8 . The fracturing fluid of claim 1 , wherein the proppant particulates have an average particle size distribution in the range of 70 microns (μm) to 600 μm, depending on a grinding or milling technique used to process the delayed coke material.
9 . The fracturing fluid of claim 1 , wherein the proppant particulates are further composed of a fluid coke material or a flexicoke material, or some combination thereof, in addition to the delayed coke material.
10 . A method, comprising introducing a fracturing fluid into a subterranean formation, the fracturing fluid comprising a carrier fluid and proppant particulates composed of delayed coke material.
11 . The method of claim 10 , further comprising depositing at least a portion of the proppant particulates within one or more fractures in the subterranean formation.
12 . The method of claim 10 , wherein the fracturing fluid further comprises second proppant particulates composed of a material that is not the delayed coke material.
13 . The method of claim 10 , comprising providing the delayed coke material by processing delayed coke granules using at least one grinding or milling technique.
14 . The method of claim 10 , wherein the proppant particulates are further composed of a fluid coke material or a flexicoke material, or some combination thereof, in addition to the delayed coke material.
15 . The method of claim 10 , further comprising sequestering carbon in the subterranean formation in the form of the delayed coke material.
16 . The method of claim 10 , wherein the proppant particulates have an apparent density in the range of 1.0 grams per cubic centimeter (g/cm 3 ) to 2.0 g/cm 3 .
17 . The method of claim 10 , wherein the delayed coke proppant particulates have one or more of: (a) a carbon content of 82 wt % to 90 weight percent (wt %); (b) a weight ratio of carbon to hydrogen of 15:1 to 30:1; (c) a sulfur content of 2 wt % to 8 wt %; (d) a nitrogen content of 1 wt % to 2 wt %; and (e) a combined vanadium and nickel content of 100 parts per million (ppm) to 3,000 ppm.
18 . The method of claim 10 , wherein the proppant particulates have a Hardgrove Grindability Index (HGI) value of 40 to 130 .
19 . The method of claim 10 , wherein the proppant particulates have a Krumbein roundness value and a Krumbein sphericity value of ≥0.6, and wherein the Krumbein roundness value and the Krumbein sphericity value vary based on a grinding or milling technique used to process the delayed coke material.
20 . The method of claim 10 , wherein the carrier fluid is an aqueous carrier fluid.