US3205012A - Solution mining system using heat exchange tubes - Google Patents
Solution mining system using heat exchange tubes Download PDFInfo
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- US3205012A US3205012A US277217A US27721763A US3205012A US 3205012 A US3205012 A US 3205012A US 277217 A US277217 A US 277217A US 27721763 A US27721763 A US 27721763A US 3205012 A US3205012 A US 3205012A
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- panel
- heat exchange
- exchange tubes
- solution
- ore
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- 238000005065 mining Methods 0.000 title description 14
- 239000000243 solution Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 16
- 239000007864 aqueous solution Substances 0.000 claims description 8
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 6
- 229910052700 potassium Inorganic materials 0.000 claims description 6
- 239000011591 potassium Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 3
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 30
- 239000001103 potassium chloride Substances 0.000 description 21
- 235000011164 potassium chloride Nutrition 0.000 description 21
- 229910052500 inorganic mineral Inorganic materials 0.000 description 17
- 235000010755 mineral Nutrition 0.000 description 17
- 239000011707 mineral Substances 0.000 description 17
- 239000002904 solvent Substances 0.000 description 16
- 239000012267 brine Substances 0.000 description 11
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 235000002639 sodium chloride Nutrition 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 239000010442 halite Substances 0.000 description 4
- 239000003125 aqueous solvent Substances 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910000288 alkali metal carbonate Inorganic materials 0.000 description 1
- 229910001508 alkali metal halide Inorganic materials 0.000 description 1
- 150000008045 alkali metal halides Chemical class 0.000 description 1
- 229910001963 alkali metal nitrate Inorganic materials 0.000 description 1
- 229910052936 alkali metal sulfate Inorganic materials 0.000 description 1
- 150000001642 boronic acid derivatives Chemical class 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000009740 moulding (composite fabrication) Methods 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/28—Dissolving minerals other than hydrocarbons, e.g. by an alkaline or acid leaching agent
- E21B43/281—Dissolving minerals other than hydrocarbons, e.g. by an alkaline or acid leaching agent using heat
Definitions
- the present invention generally relates to solubilizing Water-soluble minerals in a subterranean formation and removing the minerals so solubilized.
- the present invention relates to a method for efiiciently removing potassium chloride from a sylvinite ore panel.
- a mineral soluble in water is sometimes mined by pumping water or other dilute aqueous solution into a subterranean formation containing the mineral, thereby dissolving the mineral in situ, and pumping out the resulting aqueous solution containing the dissolved mineral.
- the mining of alkali metal halides, carbonates, nitrates, sulfates and borates employing Water illustrates this operation.
- the most common method of dissolving the mineral in situ employs an arrangement of concentric pipes inserted into a well penetrating the mineral stratum, the inner pipe usually being the input conduit and the outer pipe being the output conduit.
- Another method employs two or more separate Wells which penetrate the same soluble mineral bearing stratum, of which at least one well is an input well and at least one other well is an output well.
- Communication can be provided between the input and output Wells by hydraulically fracturing the formation, i.e., by injecting a uid into one of the wells at sulcient pressure to produce cracks or fissures in the formation, at least some of such fissures incepting both the input and output wells. FluidV is then circulated down the input well, along a fissure to the output well and out the output well.
- the method of this invention comprises driving entries around the perimeter of a panel of soluble mineral, such as sylvinite, inserting an input conduit into one wall of the panel and an outlet conduit into another wall of the panel, passing an aqueous solvent which is unsaturated with respect to sylvite through the ore panel between the input conduit and the output conduit, inserting a plurality of heat exchange tubes preferably sub stantially parallel to the course of ow between the input conduit and output conduit, and forcing steam through the heat exchange tubes.
- the direction of flow of the steam is preferably countercurrent to the direction of flow of the solvent.
- FIG. l is a plan View, in section, of a substantially horizontal ore panel in which a solution mining operation is carried out in accordance with this invention.
- FIG. 2 is an elevational view, in section, in the plane 2 2 of FIG. 1.
- Ore panel 10 is bounded on one side by entry 12, and on the other side by entry 14. These entries are made by means of conventional mining machinery.
- a plurality of holes are drilled through the ore panel, input casing 16 being inserted at one end of a hole of relatively large diameter and output casing 18 is provided at the opposite end of the same hole.
- Two heating exchange tubes 20 and 22 are inserted in holes of smaller diameter than that provided for the inlet casing 16 and the outlet casing 18.
- a third heat exchange tube 24 passes through casings 16 and 18. These heat exchange tubes connect through riser tubes such as riser tubes 26 and 2S to output header 30 and input header 32.
- a solvent for the ore to be recovered from ore panel 10 is introduced through input casing 16 into the ore panel.
- the solvent is removed from the ore panel through' output casing 18, and conveyed to an ore recovery plant from which it is recycled to input casing 16.
- the circulation in the panel of solvent which is unsaturated in the mineral to be produced causes the dissolution of mineral and the growth of a cavity such as cavity 36.
- Steam is introduced through input header 32 and cooled steam and water is removed through output header 30.
- the ow of heating medium, steam, is in a direction substantially parallel with, but countercurrent to, the direction of solvent flow in the ore panel.
- the ore panel is rst provided with input and output casings as shown in FIG. 1, and with a plurality of heat exchange tubes which lie in a substantially horizontal plane.
- One of the heat exchange tubes is preferably concentric with the input and output casings, as is the heat exchange tube 22, shown in FIG. 1.
- Sylvinite generally occurs in substantially horizontal strata of large horizontal dimensions but of small vertical dimensions. Thus, a typical stratum may be only five feet in height. Such narrow starta are diilicult to mine by means of conventional mining machinery.
- an aqueous brine ICC n 5J is injected into the sylvinite panel by means of input conduit 16.
- the aqueous solvent is preferably injected at a suitable high temperature, such as 90 C.
- the temperature of the solvent on reaching the output conduit would be substantially less, say 50 C., if not heat were supplied to the solvent in the ore panel. This is due to the dissipation of heat by conduction and also because of the cooling effect which, the relatively high negative heat of solution which sylvite exerts upon the solvent.
- steam at a temperature of 150 C. and 30 p.s.i.a. is introduced into input header 32 and circulated through the heat exchange tubes.
- the invention is applicable to the mining of any soluble mineral by utilizing a suitable solvent in which the mineral displays the requisite solubility. While the invention has been described with reference to the recovery of sylvite from a sylvinite ore panel, which ore panels generally lie in substantially horizontal planes, it will be apparent that the method of this invention is applicable to the recovery of minerals from ore panels disposed at any conventional dip and strike, or even from substantially vertical ore panels. It will be found most convenient to place the input and output conduits to provide circulation in the direction of the greater dimension of the ore panel.
- the heat exchange tubes be in a direction parallel to the direction of flow of solvent in the ore panel, such is not necessary. It will also he apparent that the direction of flow of steam through the heat exchange tubes need not necessarily be countercurrent to the direction of flow of solvent, although a more even heating of the solvent and more economical utilization of heat can be obtained by countercurrent How. It will also be evident that heating fluids other than steam can be utilized.
- a method for the solution mining of a sylvinite ore panel which comprises driving entries around the perimeter of the panel to thereby define a panel having substantially vertical walls, inserting a plurality of heat exchange tubes substantially horizontally through said panel, inserting an inlet casing into one Wall of said panel and an outlet casing in a wall of said panel substantially opposite to the wall into which said inlet casing is inserted, passing a Huid at an elevated temperature through said heat exchange tubes, introducing an aqueous solution substantially unsaturated with respect to potassium through said inlet casing into said panel and withdrawing an aqueous solution containing more potassium than the incoming solution through said outlet casing thereby form ing a solution cavity within said panel as potassium is dissolved in the aqueous solution and withdrawn from said panel, at least one of said heat exchange tubes passing through said solution cavity and maintaining substantially all of the solution in said solution cavity at an elevated temperature by heat exchange with the iuid in said heat exchange tubes.
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
w. B. DANCY 3,205,012
SOLUTION MINING SYSTEM USING HEAT EXCHANGE TUBES Sept. 7, 1965 Filed May l, 1965 FI E.
Z 5 y i FUER United States Patent O 3,205,012 SOLUTION MINING SYSTEM USING HEAT EXCHANGE TUBES William B. Danny, 2435 Jonla Ave., Lakeland, Fla. Filed May 1, 1963, Ser. No. 277,217 3 Claims. (Cl. 299-4) The present invention generally relates to solubilizing Water-soluble minerals in a subterranean formation and removing the minerals so solubilized. In a particular aspect the present invention relates to a method for efiiciently removing potassium chloride from a sylvinite ore panel.
A mineral soluble in water is sometimes mined by pumping water or other dilute aqueous solution into a subterranean formation containing the mineral, thereby dissolving the mineral in situ, and pumping out the resulting aqueous solution containing the dissolved mineral. The mining of alkali metal halides, carbonates, nitrates, sulfates and borates employing Water illustrates this operation.
The most common method of dissolving the mineral in situ employs an arrangement of concentric pipes inserted into a well penetrating the mineral stratum, the inner pipe usually being the input conduit and the outer pipe being the output conduit. Another method employs two or more separate Wells which penetrate the same soluble mineral bearing stratum, of which at least one well is an input well and at least one other well is an output well. Communication can be provided between the input and output Wells by hydraulically fracturing the formation, i.e., by injecting a uid into one of the wells at sulcient pressure to produce cracks or fissures in the formation, at least some of such fissures incepting both the input and output wells. FluidV is then circulated down the input well, along a fissure to the output well and out the output well.
Previously proposed processes for the solution mining of sylvinite have generally met with failure because, in the absence of heat, it was necessary to use water or a very dilute brine to dissolve sylvite from the formation. In the course of dissolving sylvite, substantial quantities of halite are dissolved which must be separated from the sylvite in relatively expensive evaporation and crystallization operations to obtain sylvite of commercial quality. For example, if the brine recovered from the solution cavity is saturated with sylvite and halite at 30 C., about six parts of Water must be evaporated to produce one part of potassium chloride. Two parts of sodium chloride per part of potassium chloride are crystallized. This sodium chloride contaminant must be separated from the evaporated brine prior to crystallization of the potassium chloride.
In view of the above diculties encountered in solution mining in the absence of heating it has been proposed to heat the incoming water or dilute brine. Such previously proposed processes have also generally failed. When the solvent brine, prior to being introduced into the solution cavity was heated to effect selective dissolution ofthe potassium chloride from the sylvinite ore body, a sutl'iciently high temperature inside the cavity could not be maintained because heat was dissipated throughout the sylvinite ore body. Also, the solution of potassium chloride is endotherrnic, that is, potassium chloride has a relatively high negative heat of sodium (106 B.t.u./lb.), which also tends to cool the system substantially.
It is an object of the present invention to provide a new method for the solution mining water, soluble minerals in a subterranean formation.
It is another object of the invention to provide a method for eificiently removing potassium chloride from a subterranean sylvinite ore body.
It is a specific object of the present invention to provide a solution mining method for eiliciently removing potassium chloride from a sylvinite ore panel.
These and other objects and advantages of the present invention will be apparent as the description of the in- Vention progresses.
Briefly, the method of this invention comprises driving entries around the perimeter of a panel of soluble mineral, such as sylvinite, inserting an input conduit into one wall of the panel and an outlet conduit into another wall of the panel, passing an aqueous solvent which is unsaturated with respect to sylvite through the ore panel between the input conduit and the output conduit, inserting a plurality of heat exchange tubes preferably sub stantially parallel to the course of ow between the input conduit and output conduit, and forcing steam through the heat exchange tubes. The direction of flow of the steam is preferably countercurrent to the direction of flow of the solvent. By heat transfer between the steam and the solvent the temperature of the solvent is maintained at a suitable level, such as C., for the solution mining of the mineral.
The invention is best described with reference to the drawing, of which,
FIG. l is a plan View, in section, of a substantially horizontal ore panel in which a solution mining operation is carried out in accordance with this invention.
FIG. 2 is an elevational view, in section, in the plane 2 2 of FIG. 1.
A solvent for the ore to be recovered from ore panel 10 is introduced through input casing 16 into the ore panel. The solvent is removed from the ore panel through' output casing 18, and conveyed to an ore recovery plant from which it is recycled to input casing 16. The circulation in the panel of solvent which is unsaturated in the mineral to be produced causes the dissolution of mineral and the growth of a cavity such as cavity 36. Steam is introduced through input header 32 and cooled steam and water is removed through output header 30. The ow of heating medium, steam, is in a direction substantially parallel with, but countercurrent to, the direction of solvent flow in the ore panel.
As an example of the production of `soluble ores in accordance with a method of this invention, the application of the invention to the recovery of sylvite from a sylvinite ore panel will be described. The ore panel is rst provided with input and output casings as shown in FIG. 1, and with a plurality of heat exchange tubes which lie in a substantially horizontal plane. One of the heat exchange tubes is preferably concentric with the input and output casings, as is the heat exchange tube 22, shown in FIG. 1. Sylvinite generally occurs in substantially horizontal strata of large horizontal dimensions but of small vertical dimensions. Thus, a typical stratum may be only five feet in height. Such narrow starta are diilicult to mine by means of conventional mining machinery. Since the sylvite contained in the sylvinite ore is substantially more soluble in water at elevated temperature than is the halite contained in the sylvinite ore, an aqueous brine ICC n 5J is injected into the sylvinite panel by means of input conduit 16. The aqueous solvent is preferably injected at a suitable high temperature, such as 90 C. The temperature of the solvent on reaching the output conduit would be substantially less, say 50 C., if not heat were supplied to the solvent in the ore panel. This is due to the dissipation of heat by conduction and also because of the cooling effect which, the relatively high negative heat of solution which sylvite exerts upon the solvent.
In accordance with this invention steam at a temperature of 150 C. and 30 p.s.i.a. is introduced into input header 32 and circulated through the heat exchange tubes.
l Some steam at about 100 C. and 15 p.s.i.a. and condensate is removed through output header 30. The steam rate is controlled by means of a valve, not shown, to maintain the temperature of the aqueous solvent in the ore panel at about 90 C. The brine recovered through output conduit 18 is conveyed to a salt recovery plant in which the temperature of the brine is reduced to about 30 C. In this operation about nine tons of sylvite, substantially uncontaminated with halite, are recovered from each 100 tons of brine circulated through the ore panel. After recovery of the sylvite from the brine, the brine is again heated to 90 C. and introduced into the sylvinite ore panel through casing 16.
A number of possible variations in the operation of the processes of this invention will at once be apparent to those skilled in the art. For example, the invention is applicable to the mining of any soluble mineral by utilizing a suitable solvent in which the mineral displays the requisite solubility. While the invention has been described with reference to the recovery of sylvite from a sylvinite ore panel, which ore panels generally lie in substantially horizontal planes, it will be apparent that the method of this invention is applicable to the recovery of minerals from ore panels disposed at any conventional dip and strike, or even from substantially vertical ore panels. It will be found most convenient to place the input and output conduits to provide circulation in the direction of the greater dimension of the ore panel. While it is preferred that the heat exchange tubes be in a direction parallel to the direction of flow of solvent in the ore panel, such is not necessary. It will also he apparent that the direction of flow of steam through the heat exchange tubes need not necessarily be countercurrent to the direction of flow of solvent, although a more even heating of the solvent and more economical utilization of heat can be obtained by countercurrent How. It will also be evident that heating fluids other than steam can be utilized.
The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
1. A method for the solution mining of a sylvinite ore panel which comprises driving entries around the perimeter of the panel to thereby define a panel having substantially vertical walls, inserting a plurality of heat exchange tubes substantially horizontally through said panel, inserting an inlet casing into one Wall of said panel and an outlet casing in a wall of said panel substantially opposite to the wall into which said inlet casing is inserted, passing a Huid at an elevated temperature through said heat exchange tubes, introducing an aqueous solution substantially unsaturated with respect to potassium through said inlet casing into said panel and withdrawing an aqueous solution containing more potassium than the incoming solution through said outlet casing thereby form ing a solution cavity within said panel as potassium is dissolved in the aqueous solution and withdrawn from said panel, at least one of said heat exchange tubes passing through said solution cavity and maintaining substantially all of the solution in said solution cavity at an elevated temperature by heat exchange with the iuid in said heat exchange tubes.
2. The method in accordance with claim 1 in which said heat exchange tubes extend substantially parallel to the direction of solution W between said inlet and outlet casings.
3. The method in accordance with claim 2 in which the flow of iiuid through said heat exchange tubes is countercurrent to the direction of flow of said solvent.
References Cited by the Examiner UNITED STATES PATENTS 1,121,225 12/ 14 Bradley. 1,960,932 5/ 34 Tracy. 2,161,800 6/39 Cross. 2,625,384 l/53 Pike et al. 2,682,396 6/54 Haworth.
BENJAMIN HERSH, Primary Examiner.
Claims (1)
1. A METHOD FOR THE SOLUTION MINING OF A SYLVINITE ORE PANEL WHICH COMPRISES DRIVING ENTRIES AROUND THE PERIMETER OF THE PANEL TO THEREBY DEFINE A PANEL HAVING SUBSTANTIALLY VERTICAL WALLS, INSERTING A PLURALITY OIF HEAT EXCHANGE TUBES SUBSTANTIALLY HORIZONTAL THROUGH SAID PANEL, INSERTING AN INLET CASING INTO ONE WALL OF SAID PANEL AND AN OUTLET CASING IN A WALL OF SAID PANEL SUBSTANTIALLY OPPOSITE TO THE WALL INTO WHICH SAID INLET CASING IS INSERTED, PASSING A FLUID AT AN ELEVATED TEMPERATURE THROUGH SAID HEAT EXCHANGE TUBES, INTRODUCING AN AQUEOUS SOLUTION SUBSTANTIALLY UNSATURATED WITH RESPECT TO POTASSIUM THROUGH SAID INLET CASING INTO SAID PANEL AND WITHDRAWING AN AQUEOUS SOLUTION CONTAINING MORE POTASSIUM THAN THE INCOMING SOLUTION THROUGH SAID OUTLET CASING THEREBY FORMING A SOLUTION CAVITY WITHIN SAID PANEL AS POTASSIUM IT DISSOLVED IN THE AQUEOUS SOLUTION AND WITHDRAWN FROM SAID PANEL, AT LEAST ONE OF SAID HEAT EXCHANGE TUBES PASSING THROUGH SAID SOLUTION CAVITY AND MAINTAINING SUBSTANTIALLY ALL OF THE SOLUTION IN SAID SOLUTION CAVITY AT AN ELEVATED TEMPERATURE BY HEAT EXCHANGE WITH THE FLUID IN SAID HEAT EXCHANGE TUBES.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US277217A US3205012A (en) | 1963-05-01 | 1963-05-01 | Solution mining system using heat exchange tubes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US277217A US3205012A (en) | 1963-05-01 | 1963-05-01 | Solution mining system using heat exchange tubes |
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| Publication Number | Publication Date |
|---|---|
| US3205012A true US3205012A (en) | 1965-09-07 |
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ID=23059893
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US277217A Expired - Lifetime US3205012A (en) | 1963-05-01 | 1963-05-01 | Solution mining system using heat exchange tubes |
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| Country | Link |
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| US (1) | US3205012A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3386768A (en) * | 1966-09-29 | 1968-06-04 | Int Salt Co | Mining and refining soluble minerals |
| US3421794A (en) * | 1966-09-27 | 1969-01-14 | Int Salt Co | Solution mining and refining minerals |
| US3994340A (en) * | 1975-10-30 | 1976-11-30 | Chevron Research Company | Method of recovering viscous petroleum from tar sand |
| US3994341A (en) * | 1975-10-30 | 1976-11-30 | Chevron Research Company | Recovering viscous petroleum from thick tar sand |
| FR2329839A1 (en) * | 1975-10-30 | 1977-05-27 | Chevron Res | PROCESS FOR EXTRACTING VISCOUS OIL FROM AN UNDERGROUND FORMATION |
| US4249775A (en) * | 1978-01-18 | 1981-02-10 | British Sulphur Corp., Ltd. | Mining of sulphur |
| US8955591B1 (en) | 2010-05-13 | 2015-02-17 | Future Energy, Llc | Methods and systems for delivery of thermal energy |
| US9200505B2 (en) | 2010-08-18 | 2015-12-01 | Future Energy, Llc | Methods and systems for enhanced delivery of thermal energy for horizontal wellbores |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1121225A (en) * | 1913-11-18 | 1914-12-15 | Charles S Bradley | Method and apparatus for mining salt. |
| US1960932A (en) * | 1933-07-21 | 1934-05-29 | Solvay Process Co | Method of mining |
| US2161800A (en) * | 1937-04-10 | 1939-06-13 | Cross Roy | Mining potash |
| US2625384A (en) * | 1949-07-01 | 1953-01-13 | Fmc Corp | Mining operation |
| US2682396A (en) * | 1948-09-17 | 1954-06-29 | Potash Company | Method for mining soluble ores |
-
1963
- 1963-05-01 US US277217A patent/US3205012A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1121225A (en) * | 1913-11-18 | 1914-12-15 | Charles S Bradley | Method and apparatus for mining salt. |
| US1960932A (en) * | 1933-07-21 | 1934-05-29 | Solvay Process Co | Method of mining |
| US2161800A (en) * | 1937-04-10 | 1939-06-13 | Cross Roy | Mining potash |
| US2682396A (en) * | 1948-09-17 | 1954-06-29 | Potash Company | Method for mining soluble ores |
| US2625384A (en) * | 1949-07-01 | 1953-01-13 | Fmc Corp | Mining operation |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3421794A (en) * | 1966-09-27 | 1969-01-14 | Int Salt Co | Solution mining and refining minerals |
| US3386768A (en) * | 1966-09-29 | 1968-06-04 | Int Salt Co | Mining and refining soluble minerals |
| US3994340A (en) * | 1975-10-30 | 1976-11-30 | Chevron Research Company | Method of recovering viscous petroleum from tar sand |
| US3994341A (en) * | 1975-10-30 | 1976-11-30 | Chevron Research Company | Recovering viscous petroleum from thick tar sand |
| FR2329839A1 (en) * | 1975-10-30 | 1977-05-27 | Chevron Res | PROCESS FOR EXTRACTING VISCOUS OIL FROM AN UNDERGROUND FORMATION |
| US4037658A (en) * | 1975-10-30 | 1977-07-26 | Chevron Research Company | Method of recovering viscous petroleum from an underground formation |
| US4249775A (en) * | 1978-01-18 | 1981-02-10 | British Sulphur Corp., Ltd. | Mining of sulphur |
| US8955591B1 (en) | 2010-05-13 | 2015-02-17 | Future Energy, Llc | Methods and systems for delivery of thermal energy |
| US9200505B2 (en) | 2010-08-18 | 2015-12-01 | Future Energy, Llc | Methods and systems for enhanced delivery of thermal energy for horizontal wellbores |
| US9464514B2 (en) | 2010-08-18 | 2016-10-11 | Future Energy, Llc | Methods and systems for enhanced delivery of thermal energy for horizontal wellbores |
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