US345586A - Oil from wells - Google Patents
Oil from wells Download PDFInfo
- Publication number
- US345586A US345586A US345586DA US345586A US 345586 A US345586 A US 345586A US 345586D A US345586D A US 345586DA US 345586 A US345586 A US 345586A
- Authority
- US
- United States
- Prior art keywords
- oil
- well
- steam
- wells
- pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000003921 oil Substances 0.000 description 30
- 238000000034 method Methods 0.000 description 8
- 238000007670 refining Methods 0.000 description 7
- 239000011435 rock Substances 0.000 description 6
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- 238000004061 bleaching Methods 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 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
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010892 electric spark Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- MYWUZJCMWCOHBA-VIFPVBQESA-N methamphetamine Chemical compound CN[C@@H](C)CC1=CC=CC=C1 MYWUZJCMWCOHBA-VIFPVBQESA-N 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP 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
- E21B43/34—Arrangements for separating materials produced by the well
Definitions
- This invention relates to an improved meth d of refining oil in the wells, and to facilitate the discharge of the oil from the wells, and to separate the oil so produced according to the different gravities of the various hydrocarbon compounds of which the oil is composed.
- A represents the oil-well
- B the stratum of oil-bearing rock
- D a steam-boiler
- F a steampipe leading from the boiler into the well', and terminating in the same in proximity to the oil-bearing rock
- G the discharge-pipe,which is connected with the upper end of the casing, and H a closed tank or receptacle which receives the oil from the discharge-pipe G.
- the steam-boiler is constructed of a large number of small tubes or spheres made of the proper dimensions. to stand a pressure of from one thousand to fifteen hundred pounds per square inch. I prefer to employ a pressure of about fifteen hundred pounds per square inch; but a lower pressure may be employed.
- This compound may be employed either in a dry state or as a solution, and it may be injected into the steam-pipe by a suitable pump or by an aspirator, or it may be delivered into the well by a separate pipe.
- the bleached and refined oil is forced upwardly through the casing of the well by the act-ion of the steam, vapor, and gases injected into and generated in the well, and delivered through the discharge-pipe G to the receivingtank H.
- the discharge-pipe G is preferably surrounded by a water'jacket, I, which is provided with a water-supply at its lower end and a water-escape at its upper end, and through which water is caused to circulate for the purpose of cooling the oil and the vapor which pass through the discharge pipe G.
- the latter may be made tapering from the well toward the receivi ng-tank H,to reduce the area or cross-section in the pipe gradually and in the same measure as the contents of the pipe become denser by cooling.
- the receivingtank H is preferably provided with a steamcoil, L, whereby the oil contained therein is heatedfirst t0 the proper temperature for driving off the naphtha and similar light hydrocarbons, which are collected in a receptacle, K. ⁇ Vhen this has been accomplished, the temperature is raised so as to drive off the illuminating-oil, which is collected in a receptacle, M.
- the temperature is raised so as to drive off the heavy lubricating-oil, which is collected in a receptacle, N, when the residue is discharged from the receiving-tank H, and the latter prepared to receive another charge of oil.
- a suitable number of receiving-tanks are provided, so that the oil confined in the IOC well can be delivered into one tank while the distillation of the oil is being e fected in another tank. The oil is in this manner reduced in a very simple way and made ready for the market at the well, whereby the cost of transporting and storing the crude oil is to a large extent avoided.
- the herein-described method of obtaining oil from the well is especially applicable to old and abandoned wells which have ceased to produce oil in paying quantities, and my improved method will not only restore the productiveness of such wells, but also increase the yield of wells which are now operated by pumping.
- ⁇ Vhen steam is applied at a low pressure,the same resultean be attained by decomposing the steam when it issues from the pipe by means of the electric spark or heated platinum wires.
- a suitable generator of eleetricitysnch as a dynamoeleetrie machine for instance is employed, and the conducting-wires are extended from the generator into the well and properly insulated and provided with the proper appliances for directing the dynamic spark through the steam-jet, or they are provided with one or more common platinum wires arranged in the steam-jet in the well.
- the herein-described method of refining oil in the well which consists in injecting into the well steam charged or impregnated with a bleaching or refining agent, substantially as set forth.
- the hcrein'deseribed method of refining oil in the well which consists in applying a suitable bleaching or refining agent to the oil in the well, substantially as set forth.
Description
(No Model.) I a T. G. HALL. V
. METHOD OF OBTAINING OIL PROM WELLS. No. 345 586. Patented July 13, 1886.
I ju/flw Jnvmiw. a 2g minans'es. .Z Jiezome N, PETERS. Phuivulhngnphur. Wlshingion. DHC.
UNITED STATES "PATE T Grinch.
THURSTEN G. HALL, OF NlAGARA FALLS, NEWV YORK.
METHOD OF OBTAINING OIL FROM WELLS.
ilPECIF-ICATION forming part of Letters Patent No. 345,586, dated July 13, 1886.
Application filed March 27, 1883. Serial No. 89,049. (No model.)
ficatiom This invention relates to an improved meth d of refining oil in the wells, and to facilitate the discharge of the oil from the wells, and to separate the oil so produced according to the different gravities of the various hydrocarbon compounds of which the oil is composed.
My invention consists, to these ends, of the improved method which will be hereinafter fully described, and pointed out in the claims.
The accompanying drawing represents an apparatus which is used in practicing my invention. v
A represents the oil-well; B, the stratum of oil-bearing rock; 0, the casing inserted in the bore of the well; D, a steam-boiler; F, a steampipe leading from the boiler into the well', and terminating in the same in proximity to the oil-bearing rock; G, the discharge-pipe,which is connected with the upper end of the casing, and H a closed tank or receptacle which receives the oil from the discharge-pipe G.
The steam-boiler is constructed of a large number of small tubes or spheres made of the proper dimensions. to stand a pressure of from one thousand to fifteen hundred pounds per square inch. I prefer to employa pressure of about fifteen hundred pounds per square inch; but a lower pressure may be employed. The
steam issues from the end of the steam-pipe F into the well opposite the seams in the oilbearing rock,and becomes decomposed by coming in contact with the hydrocarbon compounds in the oil-bearing rock, the hydrogen of the steam combining with the parafiine and other heavy hydrocarbons, whereby the same are transformed into liquid or light oil and vapor, and the oxygen of the steam forming carbonic monoxide and dioxide with the carbon of the hydrogen carbons, which escape from the oil with the oil as gases, and which aid in driving the 011 and vapor to the surface. The high pressure and temperature of the steam causes the steam to thoroughly permeate the pores and seams of the oil-bearing rock,
thereby opening the same and causing the oil to flow from all the surrounding parts of the rock into the well, in which it is forced upwardly by the pressure of the steam and of the vapors and gases which are generated by the steam in the well. The steam which is injected into the well is charged with a com pound which has the effect of bleaching or refining the oil. I prefer a compound composed of eighty-eight parts of chloride of sodium, ten parts of flour of sulphur, and two parts of chloride 'of ammonium for this purpose; but other bleachingand refiningcompounds maybe used, if desired. This compound may be employed either in a dry state or as a solution, and it may be injected into the steam-pipe by a suitable pump or by an aspirator, or it may be delivered into the well by a separate pipe. The bleached and refined oil is forced upwardly through the casing of the well by the act-ion of the steam, vapor, and gases injected into and generated in the well, and delivered through the discharge-pipe G to the receivingtank H. The discharge-pipe G is preferably surrounded by a water'jacket, I, which is provided with a water-supply at its lower end and a water-escape at its upper end, and through which water is caused to circulate for the purpose of cooling the oil and the vapor which pass through the discharge pipe G. The latter may be made tapering from the well toward the receivi ng-tank H,to reduce the area or cross-section in the pipe gradually and in the same measure as the contents of the pipe become denser by cooling. The receivingtank H is preferably provided with a steamcoil, L, whereby the oil contained therein is heatedfirst t0 the proper temperature for driving off the naphtha and similar light hydrocarbons, which are collected in a receptacle, K. \Vhen this has been accomplished, the temperature is raised so as to drive off the illuminating-oil, which is collected in a receptacle, M. \Vhen this has been accomplished, the temperature is raised so as to drive off the heavy lubricating-oil, which is collected in a receptacle, N, when the residue is discharged from the receiving-tank H, and the latter prepared to receive another charge of oil. A suitable number of receiving-tanks are provided, so that the oil confined in the IOC well can be delivered into one tank while the distillation of the oil is being e fected in another tank. The oil is in this manner reduced in a very simple way and made ready for the market at the well, whereby the cost of transporting and storing the crude oil is to a large extent avoided.
The herein-described method of obtaining oil from the well is especially applicable to old and abandoned wells which have ceased to produce oil in paying quantities, and my improved method will not only restore the productiveness of such wells, but also increase the yield of wells which are now operated by pumping. \Vhen steam is applied at a low pressure,the same resultean be attained by decomposing the steam when it issues from the pipe by means of the electric spark or heated platinum wires. For this purpose a suitable generator of eleetricitysnch as a dynamoeleetrie machine, for instanceis employed, and the conducting-wires are extended from the generator into the well and properly insulated and provided with the proper appliances for directing the dynamic spark through the steam-jet, or they are provided with one or more common platinum wires arranged in the steam-jet in the well.
I claim as my inve11ti0n 1. The herein-described method of refining oil in the well, which consists in injecting into the well steam charged or impregnated with a bleaching or refining agent, substantially as set forth.
2. The hcrein'deseribed method of refining oil in the well, which consists in applying a suitable bleaching or refining agent to the oil in the well, substantially as set forth.
3. The herein-described method of produc ing refined oil, which consists in injeetinginto the well steam charged with a bleaching or refining agent, and then separating the more volatile from the less volatile component hyd rocarbon combinations by distillation; substantially as set Iortn. I
T. G. IIALL.
Witnesses:
JNo. J. BONNER, Units. F. GEYER.
Publications (1)
Publication Number | Publication Date |
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US345586A true US345586A (en) | 1886-07-13 |
Family
ID=2414654
Family Applications (1)
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US345586D Expired - Lifetime US345586A (en) | Oil from wells |
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US (1) | US345586A (en) |
Cited By (37)
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US2595979A (en) * | 1949-01-25 | 1952-05-06 | Texas Co | Underground liquefaction of coal |
US4445499A (en) * | 1976-11-01 | 1984-05-01 | Sunstore Kommanditbolag | Ground-storage of heat such as solar heat |
US4530401A (en) * | 1982-04-05 | 1985-07-23 | Mobil Oil Corporation | Method for maximum in-situ visbreaking of heavy oil |
US4679598A (en) * | 1985-03-20 | 1987-07-14 | The British Petroleum Company P.L.C. | Subsea pipeline bundle |
US4880040A (en) * | 1988-09-16 | 1989-11-14 | Raymond Pierson | Liquid petroleum confinement system |
US20030079877A1 (en) * | 2001-04-24 | 2003-05-01 | Wellington Scott Lee | In situ thermal processing of a relatively impermeable formation in a reducing environment |
US20030080604A1 (en) * | 2001-04-24 | 2003-05-01 | Vinegar Harold J. | In situ thermal processing and inhibiting migration of fluids into or out of an in situ oil shale formation |
US20030098149A1 (en) * | 2001-04-24 | 2003-05-29 | Wellington Scott Lee | In situ thermal recovery from a relatively permeable formation using gas to increase mobility |
US20030155111A1 (en) * | 2001-04-24 | 2003-08-21 | Shell Oil Co | In situ thermal processing of a tar sands formation |
US20030173085A1 (en) * | 2001-10-24 | 2003-09-18 | Vinegar Harold J. | Upgrading and mining of coal |
US20030173081A1 (en) * | 2001-10-24 | 2003-09-18 | Vinegar Harold J. | In situ thermal processing of an oil reservoir formation |
US20030196801A1 (en) * | 2001-10-24 | 2003-10-23 | Vinegar Harold J. | In situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well |
US20050269077A1 (en) * | 2004-04-23 | 2005-12-08 | Sandberg Chester L | Start-up of temperature limited heaters using direct current (DC) |
US7011154B2 (en) | 2000-04-24 | 2006-03-14 | Shell Oil Company | In situ recovery from a kerogen and liquid hydrocarbon containing formation |
US7073578B2 (en) | 2002-10-24 | 2006-07-11 | Shell Oil Company | Staged and/or patterned heating during in situ thermal processing of a hydrocarbon containing formation |
US7090013B2 (en) | 2001-10-24 | 2006-08-15 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce heated fluids |
US7104319B2 (en) | 2001-10-24 | 2006-09-12 | Shell Oil Company | In situ thermal processing of a heavy oil diatomite formation |
US7121342B2 (en) | 2003-04-24 | 2006-10-17 | Shell Oil Company | Thermal processes for subsurface formations |
US7165615B2 (en) | 2001-10-24 | 2007-01-23 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden |
US20070045266A1 (en) * | 2005-04-22 | 2007-03-01 | Sandberg Chester L | In situ conversion process utilizing a closed loop heating system |
US20070108201A1 (en) * | 2005-04-22 | 2007-05-17 | Vinegar Harold J | Insulated conductor temperature limited heater for subsurface heating coupled in a three-phase wye configuration |
US20080064289A1 (en) * | 2005-09-09 | 2008-03-13 | Mcanulty Roy E | Flexible toss toy |
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US20090194333A1 (en) * | 2007-10-19 | 2009-08-06 | Macdonald Duncan | Ranging methods for developing wellbores in subsurface formations |
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US20100147521A1 (en) * | 2008-10-13 | 2010-06-17 | Xueying Xie | Perforated electrical conductors for treating subsurface formations |
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0
- US US345586D patent/US345586A/en not_active Expired - Lifetime
Cited By (284)
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US2595979A (en) * | 1949-01-25 | 1952-05-06 | Texas Co | Underground liquefaction of coal |
US4445499A (en) * | 1976-11-01 | 1984-05-01 | Sunstore Kommanditbolag | Ground-storage of heat such as solar heat |
US4530401A (en) * | 1982-04-05 | 1985-07-23 | Mobil Oil Corporation | Method for maximum in-situ visbreaking of heavy oil |
US4679598A (en) * | 1985-03-20 | 1987-07-14 | The British Petroleum Company P.L.C. | Subsea pipeline bundle |
US4880040A (en) * | 1988-09-16 | 1989-11-14 | Raymond Pierson | Liquid petroleum confinement system |
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