US1877504A - Treatment of deep wells - Google Patents
Treatment of deep wells Download PDFInfo
- Publication number
- US1877504A US1877504A US620292A US62029232A US1877504A US 1877504 A US1877504 A US 1877504A US 620292 A US620292 A US 620292A US 62029232 A US62029232 A US 62029232A US 1877504 A US1877504 A US 1877504A
- Authority
- US
- United States
- Prior art keywords
- well
- acid
- oil
- treatment
- per cent
- 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
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- 239000002253 acid Substances 0.000 description 37
- 239000000243 solution Substances 0.000 description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 21
- 238000000034 method Methods 0.000 description 20
- 239000003921 oil Substances 0.000 description 16
- 230000015572 biosynthetic process Effects 0.000 description 11
- 239000011435 rock Substances 0.000 description 11
- 229910052500 inorganic mineral Inorganic materials 0.000 description 10
- 239000011707 mineral Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 239000003129 oil well Substances 0.000 description 9
- 239000012267 brine Substances 0.000 description 8
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 150000002739 metals Chemical class 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000002585 base Substances 0.000 description 6
- 230000002401 inhibitory effect Effects 0.000 description 6
- 150000001495 arsenic compounds Chemical class 0.000 description 5
- 239000012530 fluid Substances 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- DJHGAFSJWGLOIV-UHFFFAOYSA-N Arsenic acid Chemical compound O[As](O)(O)=O DJHGAFSJWGLOIV-UHFFFAOYSA-N 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 3
- 229910052785 arsenic Inorganic materials 0.000 description 3
- 229940000488 arsenic acid Drugs 0.000 description 3
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000006028 limestone Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- -1 alkali metal salts Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- XTEGARKTQYYJKE-UHFFFAOYSA-N chloric acid Chemical compound OCl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-N 0.000 description 2
- 229940005991 chloric acid Drugs 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000002360 explosive Substances 0.000 description 2
- 125000001477 organic nitrogen group Chemical group 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- HJTAZXHBEBIQQX-UHFFFAOYSA-N 1,5-bis(chloromethyl)naphthalene Chemical compound C1=CC=C2C(CCl)=CC=CC2=C1CCl HJTAZXHBEBIQQX-UHFFFAOYSA-N 0.000 description 1
- DJHGAFSJWGLOIV-UHFFFAOYSA-K Arsenate3- Chemical compound [O-][As]([O-])([O-])=O DJHGAFSJWGLOIV-UHFFFAOYSA-K 0.000 description 1
- 240000008104 Stachytarpheta jamaicensis Species 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 229940000489 arsenate Drugs 0.000 description 1
- GOLCXWYRSKYTSP-UHFFFAOYSA-N arsenic trioxide Inorganic materials O1[As]2O[As]1O2 GOLCXWYRSKYTSP-UHFFFAOYSA-N 0.000 description 1
- AQLMHYSWFMLWBS-UHFFFAOYSA-N arsenite(1-) Chemical compound O[As](O)[O-] AQLMHYSWFMLWBS-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000000266 injurious effect Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 108010080511 serum sodium transport inhibitor Proteins 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/54—Compositions for in situ inhibition of corrosion in boreholes or wells
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/62—Compositions for forming crevices or fractures
- C09K8/72—Eroding chemicals, e.g. acids
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S507/00—Earth boring, well treating, and oil field chemistry
- Y10S507/933—Acidizing or formation destroying
- Y10S507/934—Acidizing or formation destroying with inhibitor
Definitions
- the ment 0 deep wells such as oil, gas, brine or water wells, to increase the output therefrom. It is more ially concerned with the 5, treatment of w in which the mineral-bearing stratum consists of a limestone or other ca careous formation, or is contiguous to such a formation.
- An object of the invention is to counter- 1 act some preventable natural causes for the decline of yield of a well.
- a familiar example is the decline of production of an oil well.
- the release of pressure u n 35 then epositmay causethewellto ow naturall or a certain length of time.
- the flow gradually reeede from the initial high point to the point where natural flow does not produce a sufiicient yield, and thereafter pumpigguvlvill be resorted to, until the continued d e in on ut renders further operation unprofitable.
- resent invention relates to the treatlimestone formation is increased by treating with aguantity of an acid, such as hydrochloric aci
- the acid has the effect of attacking and dissolving the rock, thereby enlarging the cavity at the bottom of the well, or the channels and pores in the rock through which oil flows to the well..
- this method has never been generall adopted, due to the fact that the acid attac the metallic casing, pump tube, etc. about as actively as the rock, and causes serious damage thereto.
- a mineral acid referably hydie w chloric acid
- e latter upon reacting with the calcareous rock forms watersoluble salts which remain in solution and are removed from the well with the spent acid.
- a substance capable of inhibit attack of the acid upon metal surfaces e. g. 0 iron or steel, co per, e with which it comes in contact.
- the inhi iting agent we prefer to use an arsenic compound soluble in the acid solution, in exam les of which are arsenic acid, ELMO arsenic trioxide, As,0,, or a soluble arsenate or arsenite, such as the corresgionding alkali metal salts.
- the amount 0 arsenic comd added may be varied, but we have ound that from 1 to 5 per cent thereof, based upon the weight of the solution, will be satisfor the purpose.
- Other inhibitors which may be used are anides, Organic nitrogen bases'such as e, phenyl-hydre, 9e
- the acid solution is referably dded in amount calculated to the bore the well to a depth not ex the thickness of the mineral-bearing stra um.
- a charge of oil, water or other liquid suiiicient to overcome the head or pressure may be applied by other suitable means, ewg hby airpressure orbymeans ofa ump. en introduced into the bottom the well, the aiti-3w?
- hydrochloric acid solutions of 10 to per cent strength to which was added a small amount,e. g. l to 5 per cent, of an arsenic compound.
- hydrochloric acid solution was added 2 gallone of arsenic acid solution containing 21 pounds of arsenic calculated as As- O,.
- the mixed solution was charged into an oil well through the iron pump tube, being followed by a quantity of crude oil to force the acid solution out of the tube into the well. After the acid was exhausted, it was pum ed out, and thereupon regular um ing 0 the oil was resumed.
- the to notion of the well was approximately oubled with one treatment.
- the method has been used repeatedly for the treatment of low yield. or exhausted oil wells in producing territory with a resultant increase of output amountmg to as much as to 200 per cent, and in some cases wells which have ceased to flow have been brought back with a resumption of natural flow. Ihe treatment has been applied in the manner described without appreciable damage to the pump tube or well casing.
- the invention may also be employed similarly to increase the flow of gas wells and brine or water wells in cases where the mineral or water-bearing stratum, or the immediately adjacent strata, are of a limestone or calcareous formation, or of a nature such as to be acted upon and dissolved by hydrochloric acid solution.
- the ste which consists in introducin into the well an aqueous hydrochloric acid solution to which has been added a relatively small amount of an e nt capable of inhibiting action of the aci upon metals.
- the step which consists in introducing into the well an A aqueous hydrochloric acid solution to which has been added a relatively small amount of an arsenic compound capable of inhibiting action of the acid upon metals.
- a well for producing a fluid mineral product such as oil, gas, water or brine the ste which consists in mtroducin into.
- the ste which consists in mtroducin into the we a 5 to 20 per cent hydroch oric acid solution to which has been added from 1 to 5 per cent of arsenic acid.
- the method for increasing the output of an oil well which comprises introducing into the base of such well a5 to 20 per cent hydrochloric acid solution containing a relatively small amount of a corrosion inhibitor, permitting the acid to-act upon the rock formation surrounding the well cavity and with drawing the spent acid.
- the method for increasing the output of an oil well which comprises introducing into the base of such well a 5 to 20 per cent hydrochloric acid solution containing a relatively small amount of an arsenic com ound capo: ble of inhibiting action of the acid upon metals, pcrmitting'the acid to act u on the rock formation surrounding the we withdrawing the spent acid.
- the math for mcreasin the output of an oil well which comprises arging into the pump tube a quanti of a 5 to 20 per cent hydrochloric acid so ution containing a relatively small amount of a corrosion mcavity and.
- chloric acid solution to which has been added a relatively small amount of an organic nitrogen base capable of inhibiting action of the acid upon metals.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Patented Sept. 13, 1932 UNITED STATES PATENT ounce:
JOEE film urn 1088!. M031), mmn, IICHIGAH, ASBIGNOBS TO THE 139W cannon. conm, OI mum), 110316, A CORPORATION 01' HICHIGAH ma'rhin'ornmwmms- Drawing.
The ment 0 deep wells, such as oil, gas, brine or water wells, to increase the output therefrom. It is more ially concerned with the 5, treatment of w in which the mineral-bearing stratum consists of a limestone or other ca careous formation, or is contiguous to such a formation.
An object of the invention is to counter- 1 act some preventable natural causes for the decline of yield of a well. A familiar example is the decline of production of an oil well. When it is first drilled into an oilstratum, the release of pressure u n 35 then epositmay causethewellto ow naturall or a certain length of time. The flow gradually reeede from the initial high point to the point where natural flow does not produce a sufiicient yield, and thereafter pumpigguvlvill be resorted to, until the continued d e in on ut renders further operation unprofitable. many cases, however, the stoppage .of oil output is caused, not by exhaustion of the oil supply but by the building up of solid deposits 0 wax or the like in the channels an pores of the 0.3.- bea rock which obstruct and finally ma out o altogether the flow of oil to the we Various methods has been ugendlfolr open}; 3 mgu orcleanmg a oggedw oe,suc as dri'lling, shooting with explosive or b chemical treatment. The first two methodi mentioned have the disadvantage that the pump rod and tube must be remcved prior toapl thetre'atmenhinadditioiito which, 3% case of an explosive, there sdangerof ecasing. The
chemical methods heretofore proposed have either notbeen found efi'ective to clear the 4.0 hole or they-have involved the use-of corrosive ces which metal parts of the well structure.
Asan illustrati -a chemical method is describedinU iited tatesPatent 556,669,- ei cordingtowluchtbeflowofanoilwellina 7 injurious to the Application fled has 80, 10 88. lertal Io. 620,388.
resent invention relates to the treatlimestone formation is increased by treating with aguantity of an acid, such as hydrochloric aci The acid has the effect of attacking and dissolving the rock, thereby enlarging the cavity at the bottom of the well, or the channels and pores in the rock through which oil flows to the well.. In actual practice, however, this method has never been generall adopted, due to the fact that the acid attac the metallic casing, pump tube, etc. about as actively as the rock, and causes serious damage thereto.
We have now found that the last-mentioned method may be adapted for use in increasingbor restoring the flow .of oil wells by snita le modification without material injury to the casing or other metallic-parts of the well. The treatment can be carried out at less cost and with better results than any of the methods heretofore em loyed. The invention, then consists of. t e improved method hereinafter fully described and particularly pointed out in the claims.
In ca out our improved method we employ a mineral acid, referably hydie w chloric acid, inasmuch as e latter upon reacting with the calcareous rock forms watersoluble salts which remain in solution and are removed from the well with the spent acid. To the acid we add a small amount of a substance capable of inhibit attack of the acid upon metal surfaces, e. g. 0 iron or steel, co per, e with which it comes in contact. the inhi iting agent we prefer to use an arsenic compound soluble in the acid solution, in exam les of which are arsenic acid, ELMO arsenic trioxide, As,0,, or a soluble arsenate or arsenite, such as the corresgionding alkali metal salts. The amount 0 arsenic comd added may be varied, but we have ound that from 1 to 5 per cent thereof, based upon the weight of the solution, will be satisfor the purpose. Other inhibitors which may be used are anides, Organic nitrogen bases'such as e, phenyl-hydre, 9e
BEST AVAlLABLE COPY I With such strength of acid the corrosive acbe intr tube, so that the latter need not be with rawn tion thereof upon metals, particularl iron or steel can be lar 1y or substantia y inhibited by adding t ercto a relatively small amount of an arsenic compound or other inhibitin agent. Consequently, the acid can iluced into the well through the ump prior to the treatment; It is suflicient merely to pull the ump rod and valves, and to pour the acid so ution into the well throu h the tube. Due to the resence of the i ibitor there will be no su antial attack upon the pump'tube, or upon the well casing if the charge of acid rises high enough in the well to contact with thecasing.
The acid solution is referably dded in amount calculated to the bore the well to a depth not ex the thickness of the mineral-bearing stra um. In order to force the charge of acid out of the pump tube into the bore of the well against t e head of oil standing in the hole, it may be followed by a charge of oil, water or other liquid suiiicient to overcome the head or pressure may be applied by other suitable means, ewg hby airpressure orbymeans ofa ump. en introduced into the bottom the well, the aiti-3w? ti i sli or 1 ere y argmg poresandc annelsintheroc ore mn u new channela The action o f the gid n K a limestone formation causes the evclu on 01- a considerable volume of carbon dioxide Thisgasma beallowedtoescapeu;
ecasing,orthe attermaybecaptmd o thereby creatififi: igas pressure w: n the well which a forcing the acid into the pores and crevices oi the rock. Aiter the action of the acid has practicallglceased the spent solution ccntsinin the mind salts may be umped or ball out. In many cases it may desirable to repeat the treatment one or more times. By making successive additions of smaller amounts of acid solution and pumping out the spent acid between a-Ereater cumulative eflect maybecg uced anbytheuseoiasingle larger args. It is not necessary, however, to add the acid solution through the pump tu as any other convenient way may be emp oyed. For instance, the pump tube may theth be withdrawn and a dump bailer used to lowor a charge of acid into the base of the bore.
In the ract'ical use of our method in the central chigan oil field, where the oil is derived from a calcareousrock formation, l
we have successfully used hydrochloric acid solutions of 10 to per cent strength to which was added a small amount,e. g. l to 5 per cent, of an arsenic compound. For example hydrochloric acid solution was added 2 gallone of arsenic acid solution containing 21 pounds of arsenic calculated as As- O,. The mixed solution was charged into an oil well through the iron pump tube, being followed by a quantity of crude oil to force the acid solution out of the tube into the well. After the acid was exhausted, it was pum ed out, and thereupon regular um ing 0 the oil was resumed. The to notion of the well was approximately oubled with one treatment.
The method has been used repeatedly for the treatment of low yield. or exhausted oil wells in producing territory with a resultant increase of output amountmg to as much as to 200 per cent, and in some cases wells which have ceased to flow have been brought back with a resumption of natural flow. Ihe treatment has been applied in the manner described without appreciable damage to the pump tube or well casing. The invention may also be employed similarly to increase the flow of gas wells and brine or water wells in cases where the mineral or water-bearing stratum, or the immediately adjacent strata, are of a limestone or calcareous formation, or of a nature such as to be acted upon and dissolved by hydrochloric acid solution.
Other modes of applying the rinciple of our invention may em loyed instead of 0 one explained, change eing made as rerds the method herein disclosed providcd' t e step or steps stated by any of the following claims or the equivalent of such stated etc or steps be employed.
e therefore particularly point out and distinctly claim as our invention 1. In a method of increasing the output of a well for producing a fluid mineral product such as oil, gas, water or brine, the ste which consists in introducin into the well an aqueous hydrochloric acid solution to which has been added a relatively small amount of an e nt capable of inhibiting action of the aci upon metals.
2. In a method of increasing the Output of a well for producing a fluid mineral p roduct such as oil, gas, water or brine, the step which consists in introducing into the well an A aqueous hydrochloric acid solution to which has been added a relatively small amount of an arsenic compound capable of inhibiting action of the acid upon metals.
8. In a method of increasing the output of to 4500 pounds of a 15 per cent Y Ill:
a well for producing a fluid mineral product such as oil, gas, water or brine, the ste which consists in mtroducin into. the we .a 5 to 20 per cent hydr oric acid solution to which-has been added from 1 to 5 per cent of an arsenic compound capable of inhibiting action of the acid upon metals.
4. In a method of increasing the output of a well for producing a fluid mineral product such as oil, gas, water or brine, the ste which consists in mtroducin into the we a 5 to 20 per cent hydroch oric acid solution to which has been added from 1 to 5 per cent of arsenic acid.
5. The method for increasing the output of an oil well which comprises introducing into the base of such well a5 to 20 per cent hydrochloric acid solution containing a relatively small amount of a corrosion inhibitor, permitting the acid to-act upon the rock formation surrounding the well cavity and with drawing the spent acid.
6. The method for increasing the output of an oil well which comprises introducing into the base of such well a 5 to 20 per cent hydrochloric acid solution containing a relatively small amount of an arsenic com ound capo: ble of inhibiting action of the acid upon metals, pcrmitting'the acid to act u on the rock formation surrounding the we withdrawing the spent acid.
7 The method for increasihgfhe output of an oil well which comprises introducing into the base of such well a 5 to 20 per cent hydrochloric acid solution containing-l. relatively small amount of a corrosion in 'bitor, permitting the acid to act u n the rock formation surrounding the we cavity while aggplying pressure upon the solution and wi drawing the nt acid.
8. The met ed for increasin the output of an oil well which comprises arging into the pump tube a quantit of a to per cent hydrochloric acid so ution containing a relatively small amount of a corrosion inh ibitor, expelling the acid from the tube into the bore of the well by applying pressure thereon, permitting the aci to ac u n the rock formation surrounding the w cavity and withdrawin the spent acid.
The math for mcreasin the output of an oil well which comprises arging into the pump tube a quanti of a 5 to 20 per cent hydrochloric acid so ution containing a relatively small amount of a corrosion mcavity and.
chloric acid solution to which has been added a relatively small amount of an organic nitrogen base capable of inhibiting action of the acid upon metals.
11. In a method of ia'eati a well for producing a fluid mineral P not such as oil,
, water or brine the step which consists in mtroduci into the well an aqueous hydrochloric aci solution to which has been added a relatively small amount of an organic sulphur compound capable of inhibiting action of the aci upon metals.
Signed by us this 24 day of June, 1932.
- JOHN J. GREBE.
ROSS T. SANFORD.
hibitor, expelling the acid from the tube into the bore of the well by a plyin pressure thereon, permitting the aci to ac u n the rock formation surrounding the we ca'vi under pressure due to the gas genera thereb and withdrawing the spent acid.
19. n a method of trea a well for producing a dud mineral uct such as oil,
as, water or brine the p which consists in introducing into th o well an aqueous hydro- Y D I 813 LA I M E R 1,877,504.John J. Grebe and Ron T. Sanford, Midland, Mich. TREATMENT or DEEP ,Wlm. Patent dated Sept. 13, 1932,. Disclmmer filed Apr.- 2, 1945, by the ueignee, The Dow Clumiml Company. Hereby enters this disclaimer to claims 1 to 9 inclusive, of said patent.
[Ofim'al Gazette May 1, 1945.] e
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US620292A US1877504A (en) | 1932-06-30 | 1932-06-30 | Treatment of deep wells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US620292A US1877504A (en) | 1932-06-30 | 1932-06-30 | Treatment of deep wells |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1877504A true US1877504A (en) | 1932-09-13 |
Family
ID=24485358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US620292A Expired - Lifetime US1877504A (en) | 1932-06-30 | 1932-06-30 | Treatment of deep wells |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1877504A (en) |
Cited By (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2426318A (en) * | 1945-11-15 | 1947-08-26 | Stanolind Oil & Gas Co | Inhibiting corrosion |
| US2426317A (en) * | 1944-12-30 | 1947-08-26 | Stanolind Oil & Gas Co | Inhibiting well corrosion |
| US2450861A (en) * | 1945-04-16 | 1948-10-05 | Dow Chemical Co | Composition for descaling ferrous metal |
| US2467164A (en) * | 1944-07-29 | 1949-04-12 | Dow Chemical Co | Acid inhibitors |
| US2472400A (en) * | 1946-11-22 | 1949-06-07 | Pure Oil Co | Method of protecting metal surfaces against hydrogen sulfide corrosion |
| US2482104A (en) * | 1946-02-08 | 1949-09-20 | Frank E Dolian | Inhibited phosphoric acid solution |
| US2493462A (en) * | 1946-12-28 | 1950-01-03 | Stanolind Oil & Gas Co | Inhibiting corrosion in wells |
| US2499283A (en) * | 1948-01-26 | 1950-02-28 | Dow Chemical Co | Inhibited hydrochloric acid |
| US2502337A (en) * | 1944-09-28 | 1950-03-28 | Pure Oil Co | Use of fluoboric acid as a means of removing core sands from castings |
| US2524757A (en) * | 1945-05-17 | 1950-10-10 | Dow Chemical Co | Cleaning scaled vessels |
| US2635698A (en) * | 1951-03-16 | 1953-04-21 | California Research Corp | Method for inhibiting corrosion |
| US2636000A (en) * | 1951-12-22 | 1953-04-21 | California Research Corp | Corrosion inhibitor containing arsenous oxide and potassium hydroxide |
| US2635999A (en) * | 1951-12-22 | 1953-04-21 | California Research Corp | Corrosion inhibiting composition containing arsenous oxide and potassium hydroxide |
| US2635996A (en) * | 1951-03-16 | 1953-04-21 | California Research Corp | Corrosion inhibitor |
| US2635998A (en) * | 1951-05-21 | 1953-04-21 | California Research Corp | Corrosion inhibiting composition |
| US2635997A (en) * | 1951-05-21 | 1953-04-21 | California Research Corp | Corrosion inhibitor |
| US2640810A (en) * | 1950-09-14 | 1953-06-02 | Dow Chemical Co | Treatment of wells |
| US2658036A (en) * | 1950-07-19 | 1953-11-03 | Texas Acidizers Inc | Composition for preventing deposition and corrosion in oil well equipment |
| US2664398A (en) * | 1952-12-02 | 1953-12-29 | Pure Oil Co | Acidizing wells |
| US2684332A (en) * | 1950-12-29 | 1954-07-20 | California Research Corp | Corrosion inhibitor |
| US2684333A (en) * | 1950-12-29 | 1954-07-20 | California Research Corp | Corrosion inhibiting composition |
| US2721183A (en) * | 1951-10-25 | 1955-10-18 | Genesee Res Corp | Dibasic alkali metal arsenate and alkali tetraborate mixture as corrosion inhibitor for aqueous glycol composition |
| US2728727A (en) * | 1952-06-19 | 1955-12-27 | Pure Oil Co | Method and composition for inhibiting corrosion |
| US2758970A (en) * | 1953-06-10 | 1956-08-14 | American Chem Paint Co | Derivatives of rosin amines |
| US2769690A (en) * | 1952-06-23 | 1956-11-06 | Phillips Petroleum Co | Inhibiting corrosion of ferrous metals |
| US2776263A (en) * | 1945-04-16 | 1957-01-01 | Clarence F Hiskey | Corrosion inhibitors for deuterium exchange process |
| US2801697A (en) * | 1953-08-03 | 1957-08-06 | Crest Res Lab Inc | Methods and means for introducing corrosion inhibitors into oil wells |
| US2936289A (en) * | 1955-05-05 | 1960-05-10 | Olin Mathieson | Water treating composition |
| US2941949A (en) * | 1957-05-14 | 1960-06-21 | Amchem Prod | Acid baths for cleaning and pickling metal |
| US2952509A (en) * | 1958-02-03 | 1960-09-13 | Dow Chemical Co | Corrosion inhibition |
| US3049496A (en) * | 1959-04-30 | 1962-08-14 | Dow Chemical Co | Propargyl compounds as corrosion inhibitors |
| US3062748A (en) * | 1959-08-24 | 1962-11-06 | Dow Chemical Co | Inhibited aqueous acidic composition |
| US3079345A (en) * | 1959-04-30 | 1963-02-26 | Dow Chemical Co | Propargyl compounds as corrosion inhibitors |
| US3197403A (en) * | 1960-04-04 | 1965-07-27 | Continental Oil Co | Acidizing corrosion inhibitor |
| US3231480A (en) * | 1959-07-27 | 1966-01-25 | Sinclair Research Inc | Corrosion protection |
| US3251415A (en) * | 1965-04-01 | 1966-05-17 | Exxon Production Research Co | Acid treating process |
| US3261710A (en) * | 1962-05-15 | 1966-07-19 | Elmer E Waldmann | Method for removing coating of epoxyphenolic resin and polytetrafluoroethylene from metal cases |
| US4493775A (en) * | 1983-09-30 | 1985-01-15 | The Dow Chemical Company | Method and composition for corrosion |
| US4790958A (en) * | 1986-02-21 | 1988-12-13 | The Dow Chemical Company | Chemical method of ferric ion removal from acid solutions |
| US4997583A (en) * | 1988-06-29 | 1991-03-05 | Bromine Compounds Ltd. | Method for protecting carbon steel from corrosion in heavy brines |
| US5445221A (en) * | 1994-04-21 | 1995-08-29 | Plainsman Technology, Inc. | Controlling ferric ions while acidizing subterranean formations |
| WO2001083639A2 (en) | 2000-05-03 | 2001-11-08 | Sofitech N.V. | Well treatment fluids comprising chelating agents |
| US6350721B1 (en) | 1998-12-01 | 2002-02-26 | Schlumberger Technology Corporation | Fluids and techniques for matrix acidizing |
-
1932
- 1932-06-30 US US620292A patent/US1877504A/en not_active Expired - Lifetime
Cited By (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2467164A (en) * | 1944-07-29 | 1949-04-12 | Dow Chemical Co | Acid inhibitors |
| US2502337A (en) * | 1944-09-28 | 1950-03-28 | Pure Oil Co | Use of fluoboric acid as a means of removing core sands from castings |
| US2426317A (en) * | 1944-12-30 | 1947-08-26 | Stanolind Oil & Gas Co | Inhibiting well corrosion |
| US2450861A (en) * | 1945-04-16 | 1948-10-05 | Dow Chemical Co | Composition for descaling ferrous metal |
| US2776263A (en) * | 1945-04-16 | 1957-01-01 | Clarence F Hiskey | Corrosion inhibitors for deuterium exchange process |
| US2524757A (en) * | 1945-05-17 | 1950-10-10 | Dow Chemical Co | Cleaning scaled vessels |
| US2426318A (en) * | 1945-11-15 | 1947-08-26 | Stanolind Oil & Gas Co | Inhibiting corrosion |
| US2482104A (en) * | 1946-02-08 | 1949-09-20 | Frank E Dolian | Inhibited phosphoric acid solution |
| US2472400A (en) * | 1946-11-22 | 1949-06-07 | Pure Oil Co | Method of protecting metal surfaces against hydrogen sulfide corrosion |
| US2493462A (en) * | 1946-12-28 | 1950-01-03 | Stanolind Oil & Gas Co | Inhibiting corrosion in wells |
| US2499283A (en) * | 1948-01-26 | 1950-02-28 | Dow Chemical Co | Inhibited hydrochloric acid |
| US2658036A (en) * | 1950-07-19 | 1953-11-03 | Texas Acidizers Inc | Composition for preventing deposition and corrosion in oil well equipment |
| US2640810A (en) * | 1950-09-14 | 1953-06-02 | Dow Chemical Co | Treatment of wells |
| US2684333A (en) * | 1950-12-29 | 1954-07-20 | California Research Corp | Corrosion inhibiting composition |
| US2684332A (en) * | 1950-12-29 | 1954-07-20 | California Research Corp | Corrosion inhibitor |
| US2635698A (en) * | 1951-03-16 | 1953-04-21 | California Research Corp | Method for inhibiting corrosion |
| US2635996A (en) * | 1951-03-16 | 1953-04-21 | California Research Corp | Corrosion inhibitor |
| US2635997A (en) * | 1951-05-21 | 1953-04-21 | California Research Corp | Corrosion inhibitor |
| US2635998A (en) * | 1951-05-21 | 1953-04-21 | California Research Corp | Corrosion inhibiting composition |
| US2721183A (en) * | 1951-10-25 | 1955-10-18 | Genesee Res Corp | Dibasic alkali metal arsenate and alkali tetraborate mixture as corrosion inhibitor for aqueous glycol composition |
| US2635999A (en) * | 1951-12-22 | 1953-04-21 | California Research Corp | Corrosion inhibiting composition containing arsenous oxide and potassium hydroxide |
| US2636000A (en) * | 1951-12-22 | 1953-04-21 | California Research Corp | Corrosion inhibitor containing arsenous oxide and potassium hydroxide |
| US2728727A (en) * | 1952-06-19 | 1955-12-27 | Pure Oil Co | Method and composition for inhibiting corrosion |
| US2769690A (en) * | 1952-06-23 | 1956-11-06 | Phillips Petroleum Co | Inhibiting corrosion of ferrous metals |
| US2664398A (en) * | 1952-12-02 | 1953-12-29 | Pure Oil Co | Acidizing wells |
| US2758970A (en) * | 1953-06-10 | 1956-08-14 | American Chem Paint Co | Derivatives of rosin amines |
| US2801697A (en) * | 1953-08-03 | 1957-08-06 | Crest Res Lab Inc | Methods and means for introducing corrosion inhibitors into oil wells |
| US2936289A (en) * | 1955-05-05 | 1960-05-10 | Olin Mathieson | Water treating composition |
| US2941949A (en) * | 1957-05-14 | 1960-06-21 | Amchem Prod | Acid baths for cleaning and pickling metal |
| US2952509A (en) * | 1958-02-03 | 1960-09-13 | Dow Chemical Co | Corrosion inhibition |
| US3049496A (en) * | 1959-04-30 | 1962-08-14 | Dow Chemical Co | Propargyl compounds as corrosion inhibitors |
| US3079345A (en) * | 1959-04-30 | 1963-02-26 | Dow Chemical Co | Propargyl compounds as corrosion inhibitors |
| US3231480A (en) * | 1959-07-27 | 1966-01-25 | Sinclair Research Inc | Corrosion protection |
| US3062748A (en) * | 1959-08-24 | 1962-11-06 | Dow Chemical Co | Inhibited aqueous acidic composition |
| US3197403A (en) * | 1960-04-04 | 1965-07-27 | Continental Oil Co | Acidizing corrosion inhibitor |
| US3261710A (en) * | 1962-05-15 | 1966-07-19 | Elmer E Waldmann | Method for removing coating of epoxyphenolic resin and polytetrafluoroethylene from metal cases |
| US3251415A (en) * | 1965-04-01 | 1966-05-17 | Exxon Production Research Co | Acid treating process |
| US4493775A (en) * | 1983-09-30 | 1985-01-15 | The Dow Chemical Company | Method and composition for corrosion |
| US4790958A (en) * | 1986-02-21 | 1988-12-13 | The Dow Chemical Company | Chemical method of ferric ion removal from acid solutions |
| US4997583A (en) * | 1988-06-29 | 1991-03-05 | Bromine Compounds Ltd. | Method for protecting carbon steel from corrosion in heavy brines |
| US5445221A (en) * | 1994-04-21 | 1995-08-29 | Plainsman Technology, Inc. | Controlling ferric ions while acidizing subterranean formations |
| US6350721B1 (en) | 1998-12-01 | 2002-02-26 | Schlumberger Technology Corporation | Fluids and techniques for matrix acidizing |
| WO2001083639A2 (en) | 2000-05-03 | 2001-11-08 | Sofitech N.V. | Well treatment fluids comprising chelating agents |
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