US2426317A - Inhibiting well corrosion - Google Patents
Inhibiting well corrosion Download PDFInfo
- Publication number
- US2426317A US2426317A US570799A US57079944A US2426317A US 2426317 A US2426317 A US 2426317A US 570799 A US570799 A US 570799A US 57079944 A US57079944 A US 57079944A US 2426317 A US2426317 A US 2426317A
- Authority
- US
- United States
- Prior art keywords
- brine
- corrosion
- hydrogen sulfide
- cyanide
- inhibiting
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/18—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using inorganic inhibitors
- C23F11/181—Nitrogen containing compounds
-
- 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
- Y10S220/00—Receptacles
- Y10S220/917—Corrosion resistant container
-
- 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
- Y10S507/927—Well cleaning fluid
- Y10S507/932—Cleaning sulfur deposits
Definitions
- This invention relates to a method of inhibiting the corrosive action of natural gas and oil containing soluble sulfides. More particularly, the invention relates to means for inhibiting the rapid corrosion of well equipment which has heretofore occurred in producing wells where the hydrocarbon contains both brine and hydrogen sulfide.
- Crude oil containing soluble sulfides is produced in the major producing areas of the United States, and corrosion of oil field equipment is especially severe in areas where brines are produced with sour crudes,
- These corrosive sulfide brines include alkali sulfides, alkaline earth metal sulfides and acid sulfides such as hydrogen sulfide.
- Hydrogen sulfide is very soluble in water and brines, causing the brines to become very corrosive to equipment due to the active formation of iron sulfide. Hydrogen sulfide corrosion will take place in both acidic sulfide brines and in alkaline sulfide brines with pH below 9. This range embraces virtually all natural brines.
- One object of this invention is to provide a means for inhibiting the attack of metals by sour crudes containing brine. Another object is that of providing a class of materials for preventing chemical attack of metals by fiuids in both the liquid and vapor phases. A further object of this invention is to provide an effective inhibitor for use in treating produced well fluids before they enter the well tubing. Another object is to provide a system for treating the surface of metal to inhibit corrosion.
- an amount of a soluble-inhibiting substance as for example a, cyanide, and preferably sodium or potassium cyanide, is introduced into the producing well.
- the cyanide apparently reacts with the hydrogen sulfide in the presence of the brine to produce a thin protective film on the exposed metal surfaces.
- Various methods of introducing the inhibitor may be used, but in each case the inhibitor is supplied to the fluids being produced and is carried upwardly through the tubing. A protective film is thereby applied to the inner surface of the tubing and this film apparently acts to prevent the corrosion by the brine and hydrogen sulfide while producing the well.
- Panels of mild steel were cleaned of mill scale and smoothed with the finest grade of emery cloth. These panels were dried and weighed then of -metals in the presence of brine.
- the panel was removed from the -brine,'washed quickly in a 1% hydrochloric acid solution, wiped free of corrosion products with a soft cloth. washed with distilled water, dipped in alcohol, dried rapidly and reweighed. The weight loss was assumed tobe due to hydrogen sulfide corrosion.
- Iron that has been immersed in brine treated with sodium cyanide shows a resistance to corrosion by untreated hydrogen sulfide brines for about twenty-four hours. These data demonstrate the effectiveness of a cyanide in the inhibition of sulfide corrosion
- the invention is useful in the protection of subsurface equipment of oil wells. It is also contemplated that the treatment may be applied to pipe lines, storage tanks, and refinery equipment where attack by sour crude can be expected. Where smaller percentages of water are present, proportionately smaller amounts of inhibitor may be effective.
- potassium cyanide was added to alkaline sulfide brine of pH 7.5 in the ratio of 250 P. P. M. This was found to prevent hydrogen sulfide corrosion.
- the cyanide salt is most effective in preventing corrosion of alkaline brines and a suitable neutralizing agent, such as.
- sodium hydroxide or ammonium hydroxide can be added to bring the pH above about 7.
- the method of inhibiting hydrogen sulfide corrosion of metal in the presence of water comprising the step of commingling a small amount of a water-soluble cyanide with said water and hydrogen sulfide.
- the method of inhibiting the attack of metals by well fluids including sulfur compounds which comprises mixing with the well fluids a includes the step of mixing with the producing well fluids a small amount of a metal cyanide at least partially soluble in said well fluids.
- the method of inhibiting the corrosion of ferrous metals by well fluids containing hydrogen Y sulfide and brine which comprises supplying a small amount of sodium cyanide to the well fluids in a lower region of a producing well.
- the method of inhibiting the corrosion of ferrous metal well equipment by produced well fluids containing hydrogen sulfide and water the step which comprises treating the well at frequent intervals with a small amount of an alkali metal cyanide whereby the produced well fluids distribute a protective film over the metal surfaces.
- the method of inhibiting the tendency of well fluids containing hydrogen sulfide and water to corrode metal surfaces which comprises the steps of introducing a small amount of a watersoluble metalcyanide near the base of the well at spaced intervals of time while producing said well.
- the method of coating well equipment with a protective film to inhibit corrosion thereof by brine and sulfur-containing hydrocarbon well fluids which includes the step of introducing into the well a small amount of a cyanide at least partially soluble in said well fluids thereby depositing a protective film on the metal surfaces and reducing the hydrogen sulfide content of the well fluids.
- the method of inhibiting hydrogen sulfide corrosion of metal in the presence of water comprising the step of commingling a small amount of a water soluble salt of hydrocyanic acid with said water and hydrogen sulfide.
- the method of inhibiting the attack of metals by well fluids including sulfur compounds which comprises dispersing in the well fluids a small amount of a water soluble salt of hydrocyanic acid.
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Description
Patented Aug. 26, 1947 hurrah s'r a.
INHIBITING WELL CORROSION poration of Delaware No Drawing. Application December 30, 194.4, Serial No. 570,799
11 Claims.
This invention relates to a method of inhibiting the corrosive action of natural gas and oil containing soluble sulfides. More particularly, the invention relates to means for inhibiting the rapid corrosion of well equipment which has heretofore occurred in producing wells where the hydrocarbon contains both brine and hydrogen sulfide.
Crude oil containing soluble sulfides is produced in the major producing areas of the United States, and corrosion of oil field equipment is especially severe in areas where brines are produced with sour crudes, These corrosive sulfide brines include alkali sulfides, alkaline earth metal sulfides and acid sulfides such as hydrogen sulfide. Hydrogen sulfide is very soluble in water and brines, causing the brines to become very corrosive to equipment due to the active formation of iron sulfide. Hydrogen sulfide corrosion will take place in both acidic sulfide brines and in alkaline sulfide brines with pH below 9. This range embraces virtually all natural brines.
In some areas, the production is so corrosive that, after the tubing has been in use for a relatively short time, it has been necessary to pull the tubing once a week to inspect for failure. In one case, it was necessary to replace eleven joints in one string of tubing within eight months because of leaks; in another, a new string of pump rods began parting after thirty-six days of service. It will be apparent, therefore, that the cost of replacing equipment made useless by corrosion and the cost of labor involved are major factors in the future economic operation of many oil fields producing sour crude and brine.
One object of this invention, therefore, is to provide a means for inhibiting the attack of metals by sour crudes containing brine. Another object is that of providing a class of materials for preventing chemical attack of metals by fiuids in both the liquid and vapor phases. A further object of this invention is to provide an effective inhibitor for use in treating produced well fluids before they enter the well tubing. Another object is to provide a system for treating the surface of metal to inhibit corrosion. The above and other objects of my invention will become apparent to those skilled in the art as the description thereof proceeds,
For many years generally inefiective efiorts have been made by equipment manufacturers and corrosion experts to develop materials capable of withstanding hydrogen sulfide corrosion of the type to which this invention is directed. Various steel alloy tubings were tried under these corrosive conditions without apparent success, since the additional cost of the alloy did not give a corresponding additional length of service. Likewise, coatings of paint and synthetic rubber have failed to prevent metal from attack when the equipment was put in field use. Zinc plates have been installed on pump rods and in treaters as a form of cathodic protection, but this has also failed to prevent damage. Chemical treatment with sodium hydroxide, tannin, and sodium silicate, and the like involving the attempted neu tralization of the hydrogen sulfide has been tried in wells without avoiding this type of corrosion.
In carrying out the present invention, an amount of a soluble-inhibiting substance as for example a, cyanide, and preferably sodium or potassium cyanide, is introduced into the producing well. The cyanide apparently reacts with the hydrogen sulfide in the presence of the brine to produce a thin protective film on the exposed metal surfaces. Various methods of introducing the inhibitor may be used, but in each case the inhibitor is supplied to the fluids being produced and is carried upwardly through the tubing. A protective film is thereby applied to the inner surface of the tubing and this film apparently acts to prevent the corrosion by the brine and hydrogen sulfide while producing the well.
Reactions are known to take place to produce traces of new compounds, only a relatively minor proportion of the original agents reacting. This appears to be the case with the soluble cyanide and hydrogen sulfide in brines, since the major portion of the hydrogen sulfide content is unaffected but apparently does not retain its corrosive properties. Without being limited to any theory of operation, it appears that by the slow reaction of cyanide with the hydrogen sulfide in brine a new compound is produced which in turn reacts to form a molecular film on the iron which corresponds to the theoretical mechanism by which pickling agents operate.
The phenomenon was studied in the laboratory and when sodium cyanide was added to alkaline hydrogen sulfide brines there appeared to be visible signs of chemical reaction and a very small amount of insoluble precipitate formed, the reaction drifting slightly toward neutral. The cyanide reacted, but only a small portion of the dissolved hydrogen sulfide-was consumed, since the brine still showed a high content of hydrogen sulfide following the treatment.
Panels of mild steel were cleaned of mill scale and smoothed with the finest grade of emery cloth. These panels were dried and weighed then of -metals in the presence of brine.
suspended in the sulfide brine on glass hooks. After immersion for a known time, the panel was removed from the -brine,'washed quickly in a 1% hydrochloric acid solution, wiped free of corrosion products with a soft cloth. washed with distilled water, dipped in alcohol, dried rapidly and reweighed. The weight loss was assumed tobe due to hydrogen sulfide corrosion.
Data obtained by these tests are set out in the following table:
Loss in lbs.
Inhibiting Corrosion of iron by sulfide brine pggrsgfyt. power Per cent West Texas brine (control) 00286 none West Texas brine+.027 NaON 00016 95 West Texas brine+.04 NaON 00000 l West Texas brine+.06 o NaCN 00000 100 New Mexico brine (control) 0022 none New Mexico brine+.02 N aCN 0005 80 New Mexico brine+.04 a N aCN 00010 95 New Mexico brine+.06% NaON 00016 It will be apparent that if a soluble cyanide such. as sodium cyanide is added to a brine containing hydrogen sulfide, such treated brine has little or no corrosive property on metal. Iron that has been immersed in brine treated with sodium cyanide shows a resistance to corrosion by untreated hydrogen sulfide brines for about twenty-four hours. These data demonstrate the effectiveness of a cyanide in the inhibition of sulfide corrosion Thus the invention is useful in the protection of subsurface equipment of oil wells. It is also contemplated that the treatment may be applied to pipe lines, storage tanks, and refinery equipment where attack by sour crude can be expected. Where smaller percentages of water are present, proportionately smaller amounts of inhibitor may be effective. v
In another example, potassium cyanide was added to alkaline sulfide brine of pH 7.5 in the ratio of 250 P. P. M. This was found to prevent hydrogen sulfide corrosion. The cyanide salt is most effective in preventing corrosion of alkaline brines and a suitable neutralizing agent, such as.
sodium hydroxide or ammonium hydroxide, can be added to bring the pH above about 7.
The foregoing description has been with particular reference to the use of sodium cyanide as an example of the class of materials contemplated by this invention. It is to be understood, however, that soluble cyanide salts as a class or materials producing cyanides under conditions existing within a producing Well are contemplated.
The preferred embodiments of my invention described herein are for the purpose of illustration and are not intended to limit the scope of the invention, since it is apparent that the principles of my invention may be applied to analogous situations by those skilled in the art in view of the foregoing description.
What I claim is:
1. The method of inhibiting hydrogen sulfide corrosion of metal in the presence of water comprising the step of commingling a small amount of a water-soluble cyanide with said water and hydrogen sulfide.
2. The method of inhibiting the attack of metals by well fluids including sulfur compounds which comprises mixing with the well fluids a includes the step of mixing with the producing well fluids a small amount of a metal cyanide at least partially soluble in said well fluids.
4. The method of inhibiting the corrosion of ferrous metals by well fluids containing hydrogen Y sulfide and brine which comprises supplying a small amount of sodium cyanide to the well fluids in a lower region of a producing well.
5. The method of inhibiting the corrosion of ferrous metal well equipment by produced well fluids containing hydrogen sulfide and water the step which comprises treating the well at frequent intervals with a small amount of an alkali metal cyanide whereby the produced well fluids distribute a protective film over the metal surfaces.
6. The method of inhibiting the tendency of well fluids containing hydrogen sulfide and water to corrode metal surfaces which comprises the steps of introducing a small amount of a watersoluble metalcyanide near the base of the well at spaced intervals of time while producing said well.
7. The method of coating well equipment with a protective film to inhibit corrosion thereof by brine and sulfur-containing hydrocarbon well fluids which includes the step of introducing into the well a small amount of a cyanide at least partially soluble in said well fluids thereby depositing a protective film on the metal surfaces and reducing the hydrogen sulfide content of the well fluids.
8. The method of rendering metal surfaces resistant to hydrogen sulfide corrosion in the presence of brines which comprises the steps of contacting the metal surfaces with an alkaline solution of the reaction products of hydrogen sulfide and a metal'cyanide at least partially soluble in said brine.
9. The method of inhibiting corrosion of metals by fluids containing soluble sulfides which includes the addition to said fluids of a small amount of a cyanide salt which is at least partially soluble in said fluids. v
10. The method of inhibiting hydrogen sulfide corrosion of metal in the presence of water, comprising the step of commingling a small amount of a water soluble salt of hydrocyanic acid with said water and hydrogen sulfide.
11. The method of inhibiting the attack of metals by well fluids including sulfur compounds which comprises dispersing in the well fluids a small amount of a water soluble salt of hydrocyanic acid.
PAUL L. MENAUL.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Smith Sept. 5, 1944:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US570799A US2426317A (en) | 1944-12-30 | 1944-12-30 | Inhibiting well corrosion |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US570799A US2426317A (en) | 1944-12-30 | 1944-12-30 | Inhibiting well corrosion |
Publications (1)
Publication Number | Publication Date |
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US2426317A true US2426317A (en) | 1947-08-26 |
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ID=24281098
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US570799A Expired - Lifetime US2426317A (en) | 1944-12-30 | 1944-12-30 | Inhibiting well corrosion |
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US (1) | US2426317A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2510771A (en) * | 1946-11-01 | 1950-06-06 | Pure Oil Co | Method of protecting metal surfaces against hydrogen sulfide corrosion |
US2642139A (en) * | 1946-04-26 | 1953-06-16 | Stanolind Oil & Gas Co | Apparatus for treating wells |
US2700652A (en) * | 1951-02-23 | 1955-01-25 | Paul D Menaul | Inhibiting corrosion due to sulfur compounds |
US2818079A (en) * | 1954-02-23 | 1957-12-31 | Texaco Development Corp | Prevention of paraffin deposition |
US2856001A (en) * | 1956-12-24 | 1958-10-14 | Jersey Prod Res Co | Protection of wells |
US3062684A (en) * | 1957-09-03 | 1962-11-06 | Shell Oil Co | Method of inhibiting corrosion of iron and steel |
US3127932A (en) * | 1961-12-01 | 1964-04-07 | California Research Corp | Composition and method for inhibiting corrosion in oil wells |
US3199585A (en) * | 1963-03-13 | 1965-08-10 | Dow Chemican Company | Well treating method |
US5396958A (en) * | 1993-10-20 | 1995-03-14 | Jacam Chemical Partners, Ltd. | Well treating composition and method of use |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1829705A (en) * | 1925-03-12 | 1931-10-27 | Empire Oil & Refining Company | Prevention of corrosion in oil wells |
US1873084A (en) * | 1928-07-19 | 1932-08-23 | Empire Oil And Refining Compan | Method of preventing corrosion in oil wells |
US1877504A (en) * | 1932-06-30 | 1932-09-13 | Dow Chemical Co | Treatment of deep wells |
US2105672A (en) * | 1937-06-28 | 1938-01-18 | Sadtler Robert Edward | Rust preventing composition and method of rust prevention |
US2297666A (en) * | 1940-03-09 | 1942-09-29 | Shell Dev | Internal corrosion prevention in conduits |
US2357559A (en) * | 1942-08-24 | 1944-09-05 | Odessa Chemical And Equipment | Method of sweetening sour gas and preventing corrosion of oil producing wells |
-
1944
- 1944-12-30 US US570799A patent/US2426317A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1829705A (en) * | 1925-03-12 | 1931-10-27 | Empire Oil & Refining Company | Prevention of corrosion in oil wells |
US1873084A (en) * | 1928-07-19 | 1932-08-23 | Empire Oil And Refining Compan | Method of preventing corrosion in oil wells |
US1877504A (en) * | 1932-06-30 | 1932-09-13 | Dow Chemical Co | Treatment of deep wells |
US2105672A (en) * | 1937-06-28 | 1938-01-18 | Sadtler Robert Edward | Rust preventing composition and method of rust prevention |
US2297666A (en) * | 1940-03-09 | 1942-09-29 | Shell Dev | Internal corrosion prevention in conduits |
US2357559A (en) * | 1942-08-24 | 1944-09-05 | Odessa Chemical And Equipment | Method of sweetening sour gas and preventing corrosion of oil producing wells |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2642139A (en) * | 1946-04-26 | 1953-06-16 | Stanolind Oil & Gas Co | Apparatus for treating wells |
US2510771A (en) * | 1946-11-01 | 1950-06-06 | Pure Oil Co | Method of protecting metal surfaces against hydrogen sulfide corrosion |
US2700652A (en) * | 1951-02-23 | 1955-01-25 | Paul D Menaul | Inhibiting corrosion due to sulfur compounds |
US2818079A (en) * | 1954-02-23 | 1957-12-31 | Texaco Development Corp | Prevention of paraffin deposition |
US2856001A (en) * | 1956-12-24 | 1958-10-14 | Jersey Prod Res Co | Protection of wells |
US3062684A (en) * | 1957-09-03 | 1962-11-06 | Shell Oil Co | Method of inhibiting corrosion of iron and steel |
US3127932A (en) * | 1961-12-01 | 1964-04-07 | California Research Corp | Composition and method for inhibiting corrosion in oil wells |
US3199585A (en) * | 1963-03-13 | 1965-08-10 | Dow Chemican Company | Well treating method |
US5396958A (en) * | 1993-10-20 | 1995-03-14 | Jacam Chemical Partners, Ltd. | Well treating composition and method of use |
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