Fracturing propping agent and preparation method of fracturing propping agent by using oil sludge produced in exploited of oil and gas field
US-2024067869-A1 · Feb 29, 2024 · US
US9745507B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9745507-B2 |
| Application number | US-201313952090-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 26, 2013 |
| Priority date | Aug 1, 2012 |
| Publication date | Aug 29, 2017 |
| Grant date | Aug 29, 2017 |
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Synthetic ceramic proppants are described. Proppants having a monodispersity of 3-sigma distribution or lower are also described, including methods to make these proppants and methods of using these proppants.
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What is claimed is: 1. A method of making a sintered ceramic proppant comprising forming a spherical green body core comprising one or more ceramic particulate materials; wherein the sintered ceramic proppant comprises a monodispersity with a 3-sigma distribution, wherein a width of a total distribution of the sintered ceramic proppant is 5% or less of a mean particle size of the sintered ceramic proppant, wherein the 3-sigma distribution is a size distribution of the sintered ceramic proppant; wherein the sintered ceramic proppant comprises a glassy phase, wherein the glassy phase is present in an amount of 15% to 70% based on weight of the sintered ceramic proppant; wherein the sintered ceramic proppant comprises ceramic whiskers, wherein the ceramic whiskers have an average length from 1 micron to 3.5 microns, an average width from 0.1 to 0.3 microns and a whisker length distribution from 0.1 to 5; wherein 90% of the ceramic whiskers have a whisker length that is less than 5 microns, wherein the sintered ceramic proppant comprises a free alpha-alumina content of at least 20 wt % based on the weight of the sintered ceramic proppant; wherein the sintered ceramic proppant comprises an etching weight loss from 15 wt % to 30 wt % based on the weight of the sintered ceramic proppant; forming, at the same time or afterwards, a green body shell around said green body core, wherein said green body shell comprises at least one ceramic particulate material which results in a green core/shell body; sintering said green core/shell body, and, during sintering, diffusing at least a portion of said green body core into said green body shell; wherein the diffusing forms the sintered ceramic proppant having a) a central void or a plurality of hollow regions, and b) a shell. 2. The method of claim 1 , wherein said central void or hollow regions comprises at least 1% by volume of the overall volume of the sintered ceramic proppant. 3. The method of claim 1 , wherein said diffusing results in at least 5% by weight of said green body core diffusing into said shell. 4. The method of claim 1 , wherein said diffusing results in at least 10% by weight of said green body core diffusing into said shell. 5. The method of claim 1 , wherein said diffusing results in at least 50% by weight of said green body core diffusing into said shell. 6. The method of claim 1 , wherein the green body shell has a softening temperature that is higher than the softening temperature of the green body core. 7. The method of claim 1 , wherein said green body shell has a softening temperature of at least 100° C. higher than the softening temperature of the green body core. 8. The method of claim 7 , wherein the softening temperature of the green body shell is from about 300° C. to about 400° C. higher than the softening temperature of the green body core. 9. The method of claim 1 , wherein the green body shell has a porosity of at least 10% by volume based on the volume of the green body shell. 10. The method of claim 1 , wherein the green body shell has a porosity of at least 30% by volume based on the volume of the green body shell. 11. The method of claim 1 , wherein said sintered ceramic proppant has at least 10% porosity in the sintered shell. 12. The method of claim 1 , wherein a slurry of the ceramic particulate material has an Ohnesorge Number (Z) of from 1 to 10, wherein the Ohnesorge Number (Z) is a measure of a sprayability of the slurry. 13. The method of claim 1 , wherein a slurry of the ceramic particulate material has an Ohnesorge Number (Z) of from 2 to 10, wherein the Ohnesorge Number (Z) is a measure of a sprayability of the slurry. 14. The method of claim 1 , wherein a slurry of the ceramic particulate material has an Ohnesorge Number (Z) of from 4 to 6, wherein the Ohnesorge Number (Z) is a measure of a sprayability of the slurry. 15. The method of claim 1 , wherein the whiskers or one or more fibers are formed in-situ in said shell during said sintering and as a result of said diffusing. 16. The method of claim 1 , wherein said diffusing of the green body core or portion thereof into the shell results in a gradient of wherein a higher concentration of the core is present closer to the core than to an exterior outer surface of the proppant. 17. The method of claim 1 , wherein said spherical green body, green body shell, or both further comprise at least one nucleating agent. 18. The method of claim 1 , wherein said ceramic particulate materials comprise cordierite, mullite, bauxite, silica, spodumene, silicon oxide, aluminum oxide, sodium oxide, potassium oxide, calcium oxide, zirconium oxide, lithium oxide, iron oxide, spinel, steatite, a silicate, a substituted alumino silicate clay, an inorganic nitride, an inorganic carbide, a non-oxide ceramic or any combination thereof. 19. The method of claim 1 , wherein said ceramic particulate materials comprise one or more sedimentary materials or synthetically produced materials or both. 20. The method of claim 1 , wherein said spherical green body core and said green body shell are in the absence of igneous or metamorphic materials. 21. The plurality of sintered ceramic proppants of claim 1 , wherein said sintered ceramic proppants have less than 1% by weight of proppant of igneous or metamorphic materials. 22. The method of claim 1 , wherein the green body or a portion thereof has a density, as measured by a gas pycnometer, such that the average density (g/cm3) does not alter by more than 1% between the density of the whole green body compared to the density of the crushed green body. 23. The method of claim 22 , wherein the average density changes 0.005% or less. 24. The method of claim 12 , wherein one or more mobile phases are formed in droplets of the slurry that forms the green body and one phase migrates to the surface of the droplet, which causes a multi-phase droplet to form. 25. The method of claim 24 , wherein said multi-phase droplet forms a non-uniform green body of phases. 26. The method of claim 25 , wherein said non-uniform green body of phases diffuses at different rates into said shell with respect to the phases. 27. The method of claim 1 , wherein said green body core comprises at least 50% by weight, based on the weight of the green body core of glassy material, and said green body shell comprises at least 50% crystalline material. 28. The method of claim 1 , wherein said green body core comprises at least 75% by weight, based on the weight of the green body core of glassy material, and said green body shell comprises at least 75% crystalline material. 29. The method of claim 1 , wherein said green body core comprises at least 95% by weight, based on the weight of the green body core of glassy material, and said green body shell comprises at least 95% crystalline material. 30. The method of claim 1 , wherein the particles used to form the green body core are at least 10% smaller in average mean size (d50 size) compared to the mean particle size (d50 size) of the particles that form the green body shell. 31. The method of claim 1 , wherein the particles used to form the green body core are at least 50% smaller in average mean size (d50 size) compared to the mean particle size (d50 size) of the particles that form the green body shell. 32. The method of cl
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