Dispersion solution for drilling and method of extraction using the dispersion solution
US-2015315891-A1 · Nov 5, 2015 · US
US10487620B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10487620-B2 |
| Application number | US-201515527223-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 22, 2015 |
| Priority date | Nov 19, 2014 |
| Publication date | Nov 26, 2019 |
| Grant date | Nov 26, 2019 |
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A method of extracting the underground resources by pressurizing a fluid filled in an ore chute in which cracks are formed and by, further, forming or growing the cracks, the underground resources being extracted through the cracks, wherein a hydrolysis-blocking agent is introduced with pressure into the fluid to block a diverting agent that works to temporarily close the cracks.
Opening claim text (preview).
The invention claimed is: 1. A method of extracting underground resources by pressurizing a fluid filled in an ore chute in which cracks are formed and by, further, forming or growing the cracks, the underground resources being extracted through the cracks, wherein a hydrolysis-blocking agent is introduced with pressure into the fluid to block a diverting agent that works to temporarily close the cracks, wherein the hydrolysis-blocking agent is a hydrolysable resin having a glass transition temperature (Tg) lower than a temperature in an environment of extraction and a crystallization index ΔHm of not more than 70 J/g, the crystallization index ΔHm being found from a curve of temperature rise measured in the first time by using a DSC and being represented by the following formula (1), Δ Hm=ΔHm′−ΔHc (1) wherein ΔHm′ is a quantity of heat of fusion (J/g) calculated from a peak area of an endothermic peak of fusion, and ΔHc is a quantity of heat (J/g) calculated from a peak area of an exothermic peak of crystallization. 2. The method of extraction according to claim 1 , wherein the hydrolysis-blocking agent is introduced together with the diverting agent with pressure into the fluid. 3. The method of extraction according to claim 1 , wherein after the cracks have been closed at least partly with the diverting agent, the hydrolysis-blocking agent is introduced with pressure into the fluid. 4. The method of extraction according to claim 1 , wherein an aliphatic polyester is used as the diverting agent. 5. A hydrolysis-blocking agent to be added to a fluid that is filled in an ore chute, the hydrolysis-blocking agent having a crystallization index ΔHm of not more than 70 J/g, the crystallization index ΔHm being found from a curve of temperature rise measured in the first time by using a DSC and being represented by the following formula (1), Δ Hm=ΔHm′−ΔHc (1) wherein ΔHm′ is a quantity of heat of fusion (J/g) calculated from a peak area of an endothermic peak of fusion, and ΔHc is a quantity of heat (J/g) calculated from a peak area of an exothermic peak of crystallization, wherein the hydrolysis-blocking agent is a copolymerized polyoxalate in which a dibasic acid unit other than an oxalic acid has been introduced. 6. A method of extracting underground resources by pressurizing a fluid filled in an ore chute in which cracks are formed and by, further, forming or growing the cracks, the underground resources being extracted through the cracks, wherein a hydrolysis-blocking agent is introduced with pressure into the fluid to block a diverting agent that works to temporarily close the cracks, wherein the hydrolysis-blocking agent is a hydrolysable resin having a glass transition temperature (Tg) lower than a temperature in an environment of extraction and a crystallization index ΔHm of not more than 70 J/g, the crystallization index ΔHm being found from a curve of temperature rise measured in the first time by using a DSC and being represented by the following formula (1), Δ Hm=ΔHm′−ΔHc (1) wherein ΔHm′ is a quantity of heat of fusion (J/g) calculated from a peak area of an endothermic peak of fusion, and ΔHc is a quantity of heat (J/g) calculated from a peak area of an exothermic peak of crystallization, and wherein the hydrolysis-blocking agent is a copolymerized polyoxalate in which a dibasic acid unit other than an oxalic acid has been introduced. 7. The method of extraction according to claim 6 , wherein the hydrolysis-blocking agent is introduced together with the diverting agent with pressure into the fluid. 8. The method of extraction according to claim 6 , wherein after the cracks have been closed at least partly with the diverting agent, the hydrolysis-blocking agent is introduced with pressure into the fluid. 9. The method of extraction according to claim 6 , wherein an aliphatic polyester is used as the diverting agent. 10. A method of extracting underground resources by pressurizing a fluid filled in an ore chute in which cracks are formed and by, further, forming or growing the cracks, the underground resources being extracted through the cracks, wherein a hydrolysis-blocking agent is introduced with pressure into the fluid to block a diverting agent that works to temporarily close the cracks, and wherein an aliphatic polyester is used as the diverting agent. 11. The method of extraction according to claim 10 , wherein a hydrolysable resin having a glass transition temperature (Tg) lower than a temperature in an environment of extraction is used as the hydrolysis-blocking agent. 12. The method of extraction according to claim 11 , wherein the hydrolysable resin used as the hydrolysis-blocking agent has a glass transition temperature (Tg) lower than a temperature in an environment of extraction and a crystallization index ΔHm of not more than 70 J/g, the crystallization index ΔHm being found from a curve of temperature rise measured in the first time by using a DSC and being represented by the following formula (1), Δ Hm=ΔHm′−ΔHc (1) wherein ΔHm′ is a quantity of heat of fusion (J/g) calculated from a peak area of an endothermic peak of fusion, and ΔHc is a quantity of heat (J/g) calculated from a peak area of an exothermic peak of crystallization. 13. The method of extraction according to claim 12 , wherein the hydrolysis-blocking agent is a copolymerized polyoxalate in which a dibasic acid unit other than an oxalic acid has been introduced. 14. The method of extraction according to claim 10 , wherein the hydrolysis-blocking agent is introduced together with the diverting agent with pressure into the fluid. 15. The method of extraction according to claim 10 , wherein after the cracks have been closed at least partly with the diverting agent, the hydrolysis-blocking agent is introduced with pressure into the fluid.
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