US2691631A - Method of inhibiting corrosion - Google Patents
Method of inhibiting corrosion Download PDFInfo
- Publication number
- US2691631A US2691631A US221937A US22193751A US2691631A US 2691631 A US2691631 A US 2691631A US 221937 A US221937 A US 221937A US 22193751 A US22193751 A US 22193751A US 2691631 A US2691631 A US 2691631A
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- US
- United States
- Prior art keywords
- water
- corrosion
- petroleum
- contact
- liquid
- 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
- 238000005260 corrosion Methods 0.000 title claims description 43
- 230000007797 corrosion Effects 0.000 title claims description 42
- 230000002401 inhibitory effect Effects 0.000 title claims description 22
- 238000000034 method Methods 0.000 title claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 53
- 239000007788 liquid Substances 0.000 claims description 36
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 30
- VLDHWMAJBNWALQ-UHFFFAOYSA-M sodium;1,3-benzothiazol-3-ide-2-thione Chemical compound [Na+].C1=CC=C2SC([S-])=NC2=C1 VLDHWMAJBNWALQ-UHFFFAOYSA-M 0.000 claims description 29
- 229910052751 metal Inorganic materials 0.000 claims description 28
- 239000002184 metal Substances 0.000 claims description 28
- 239000003209 petroleum derivative Substances 0.000 claims description 23
- 229930195733 hydrocarbon Natural products 0.000 claims description 18
- 150000002430 hydrocarbons Chemical class 0.000 claims description 18
- 150000001875 compounds Chemical class 0.000 claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-PWCQTSIFSA-N Tritiated water Chemical compound [3H]O[3H] XLYOFNOQVPJJNP-PWCQTSIFSA-N 0.000 claims 1
- 239000003208 petroleum Substances 0.000 description 27
- YXIWHUQXZSMYRE-UHFFFAOYSA-N 1,3-benzothiazole-2-thiol Chemical compound C1=CC=C2SC(S)=NC2=C1 YXIWHUQXZSMYRE-UHFFFAOYSA-N 0.000 description 12
- 239000007789 gas Substances 0.000 description 11
- 239000003921 oil Substances 0.000 description 11
- 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 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- 230000005764 inhibitory process Effects 0.000 description 5
- 230000035515 penetration Effects 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000010779 crude oil Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000003915 liquefied petroleum gas Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- -1 ferrous metals Chemical class 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000002343 natural gas well Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/24—Organic compounds containing sulfur, selenium and/or tellurium
- C10L1/2443—Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds
- C10L1/2456—Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds sulfur with oxygen and/or nitrogen in the ring, e.g. thiazoles
-
- 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
- Y10S507/939—Corrosion inhibitor
Definitions
- This invention relates to inhibition of corrosion and relates more particularly to inhibition of corrosion of ferrous metal by liquids containing corrosive compounds associated with petroleum hydrocarbons.
- Crude petroleum oil and gas commonly contain hydrogen sulfide, organic acids, and other compounds which, in solution in water, are corrosive to ferrous metals and these same compounds are frequently contained, although to a lesser extent, in liquid petroleum products such as oils, gasoline, liquefied petroleum gases, and the like. Further, water is frequently produced concomitantly with crude petroleum oil and gas, and water may be contained in liquid petroleum products as a result of treatment in sweetening treaters, washers, and the like.
- ferrous metal equipment of producing oil and gas wells, water disposal wells, and pipe lines for the transportation of crude petroleum oil and liquid petroleum products are frequently in contact with water solutions of hydrogen sulfide, organic acids, and other corrosive compounds associated with petroleum hydrocarbons thereby giving rise to serious corrosion problems.
- corrosion of ferrous metal in contact with a liquid comprising water and containing dissolved corrosive compound associated with petroleum hydrocarbon is inhibited by admixing with the liquid sodium mercaptobenzothiazole in corrosion inhibiting amount.
- the process of the invention may be employed for the treatment of any liquid consisting of water or containing free or dissolved water which is or has been in contact with petroleum hydrocarbons and has dissolved therein corrosive compounds associated With these petroleum hydrocarbons.
- liquid petroleum hydrocarbons such as crude petroleum oil and liquid petroleum products exemplified by oils, gasoline, and liquefied petroleum gases, natural gas from a well producing liquid Water along with the gas, and waste water separated from oil or gas of which disposal is to be made by injection into a water disposal well.
- crude petroleum oil may be treated in the Well with sodium mercaptobenzothiazole to inhibit corrosion of the well equipment.
- sodium mercaptobenzothiazole may be employed to inhibit corrosion in natural gas wells.
- the water may be treated with sodium mercaptobenzothiazole if the oil or gas fromwhich the water was separated was not treated previously in the Well or if additional treatment is desired.
- Crude petroleum oil or liquid petroleum products to be transported in pipe lines may also be treated in accordance with the invention.
- liquid petroleum hydrocarbons such as crude petroleum oils and liquid petroleum products, will not contain a free water phase at the time they enter the pipe line system. However, they may contain dissolved water and a free water phase will subsequently form as a result of condensation due to cooling by lowering of atmospheric temperature or by passage through sections of the pipe line at a lower than normal temperature, such as sections of the pipe line located under a lake or river.
- the concentration of sodium'mercaptobenzothiazole to be employed may be between about. 1
- the concentration of sodium mercaptobenzothiazole to be employed will depend upon the amount of corrosive compounds in the liquid and the extent to which corrosion is to be inhibited. Generally, satisfactory results are obtainedwhere the sodium mercaptobenzothiazole. isxemployedain an amount between: aboutt50 andQlOQ' pants-per. million. by weight .ofwtheliquidi However; the exact concentrationto be employed in.
- each particular case to obtain.the'desireddegreeof inhibition of corrosion-:with minimum: concentration of sodium mercaptobenzothiazole may; bedetermined by immersing testpieces .of the same kind of ferrous metaliwhose'corrosion' is to be inhibited in samples: of the liquid to :be treated to which-have been added :varying amounts. of 'sodiummercaptobenzothiazole, andzcomparing-the extent of corrosion of;.eachrtestpieee-after a suitable immersiontime .with the amount of sodium' mercaptobenzothiazole in the samples of liquid.
- the'sodium mercaptobenzothiazole may be intro quizzed into the wellbetween-the'tubing and the casing.v Gas-Wells may be similarly treated; the sodium-mercaptobenzothiazole admixingwith the water at the bottom of the well and inhibiting corrosion of ferrous metal equipment of the well contactedby th water lifted upwardly by the flow of gas.
- Crude-oil or liquid petroleum-products :to-be transported inapipe line system may betreated by adding .sodium mercaptobenzothiazole thereto-prior.- to-or at thetime of entering the :pipe line-system or may be-added subsequent toentering the pipeline systemibyinjecting into the pipelinesystem at a desired point or points.
- Waste wateninjected .into water disposal .wells may @be:treatedbyadmixing the sodium mercaptobenzothiazole therewith prior--to injection of. the .water intothe disposal well. If thecrude oilor. gas .fromwhich the wateris separatedhas been previously treated. with. sodium. mercaptobenzothiazole.
- the .water may ,-contain,.-suflicient with sodium; mercaptobenzothiazole 4 sodium mercaptobenzothiazole to inhibit corrosion and no further treatment will be necessary. However, if insufficient sodium mercaptobenzothiazole is contained in the water, an additional amount may be added.
- Example I In an oilnwell in the Brownfield District in Texas producing on the average 38 barrels of crude oil and 5 barrels of water per day, the ferrous: metal equipment in contact with the produced well liquidsi was being corroded at a rate of 0.0015 inch of penetration per year. This well was treatedbypumping sodium mercaptobenzothiazole in water solution between the tubing and the casing in amounts such that the concentration of sodium mercaptobenzothiazole in the total well liquids was 100 parts per million by weight.” Thetreatment-was-continued for six months.
- Example II Inanother wellin the same district producing on the average 38barrels of. crude oil and28 barrelsof. .water per day,,. the corrosion rate was 0.0078 inch.of..penetration.per year. Treatment in the amount of .10 parts .per millionv by weight of the totalwell liquidsswas. instituted and continued for two months. The corrosion rate was reduced to 0.0037 inch of. penetration per year, a decrease of. 53. percent. Thereafter, the concentration of sodium. mercaptobenzothiazole was increased to 100 parts per millionby weight .of the'total well liquidsand continued fora period of four months. The corrosionrate .was. reduced to 0.0023 .inch of penetration per. year, a decrease .of. 69 percent.
- the process for inhibitingcorrosion of ferrous metalin a petroleum-hydrocarbon well in contact with a. petroleum. hydrocarbon-well fluid containing water, saidwaterprior to contact with said ferrous metal having extracted from said petroleum hydrocarbon well fluid a water-soluble compound corrosive to said ferrous metal, which process comprises introducing into said well and admixing therein with said petroleum hydrocarbon well fiuid prior to contact of said petroleum hydrocarbon well fluid with said ferrous metal as the sole corrosion inhibiting agent sodium mercaptobenzothiazole in corrosion inhibiting amount.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Description
petroleum products.
Patented Oct. 12, 1954 UNITED STATES TNT rOFFlCE assignments, to
Socony-Vacuum Oil Company,
Incorporated, New York, N. Y., a corporation of New York No Drawing. Application April 19, 1951,
Serial No. 221,937
7 Claims. 1
This invention relates to inhibition of corrosion and relates more particularly to inhibition of corrosion of ferrous metal by liquids containing corrosive compounds associated with petroleum hydrocarbons.
Crude petroleum oil and gas commonly contain hydrogen sulfide, organic acids, and other compounds which, in solution in water, are corrosive to ferrous metals and these same compounds are frequently contained, although to a lesser extent, in liquid petroleum products such as oils, gasoline, liquefied petroleum gases, and the like. Further, water is frequently produced concomitantly with crude petroleum oil and gas, and water may be contained in liquid petroleum products as a result of treatment in sweetening treaters, washers, and the like. Thus, the ferrous metal equipment of producing oil and gas wells, water disposal wells, and pipe lines for the transportation of crude petroleum oil and liquid petroleum products are frequently in contact with water solutions of hydrogen sulfide, organic acids, and other corrosive compounds associated with petroleum hydrocarbons thereby giving rise to serious corrosion problems.
It is an object of this invention to inhibit corrosion of ferrous metal in contact with water containing dissolved corrosive compounds associated with petroleum hydrocarbons. It is another obJ'ect of this invention to inhibit corrosion of ferrous metal in contact with water in admixture with petroleum compounds. It is another object of this invention to inhibit corrosion of ferrous metal equipment in oil and gas wells, wells for the disposal of water produced concomitantly with oil and gas, and the like. It is another object of this invention to inhibit internal corrosion in pipe line systems for the transportation of crude petroleum oil and liquid These and other objects of the invention will become apparent from the following description thereof.
In accordance with the invention, corrosion of ferrous metal in contact with a liquid comprising water and containing dissolved corrosive compound associated with petroleum hydrocarbon is inhibited by admixing with the liquid sodium mercaptobenzothiazole in corrosion inhibiting amount.
I have found that the admixture of sodium mercaptobenzothiazole with liquids comprising water containing corrosive compounds associated with petroleum hydrocarbons is highly effective for inhibiting corrosion of tubing, casing, liners, pumps, valves, pipes, storage tanks, and other 2 ferrous metal equipment employed in oil and gas wells, water disposal wells, and pipe line systems for the transportation of liquid petroleum hydrocarbons such as crude oil or liquid petroleum products. Sodium mercaptobenzothiazole is water soluble. Therefore, it will accompany the water in a liquid in which it is admixed and will concentrate in a free water phase where the water is in admixture with liquid petroleum hydrocarbons. Accordingly, sodium mercaptobenzothiazole will provide inhibition of corrosion of ferrous metal equipment at points in contact with water where corrosion tends to be most severe. By ferrous metal equipment, I mean any equipment made of iron or an alloy containing iron.
The process of the invention may be employed for the treatment of any liquid consisting of water or containing free or dissolved water which is or has been in contact with petroleum hydrocarbons and has dissolved therein corrosive compounds associated With these petroleum hydrocarbons. Included among these liquids are liquid petroleum hydrocarbons, such as crude petroleum oil and liquid petroleum products exemplified by oils, gasoline, and liquefied petroleum gases, natural gas from a well producing liquid Water along with the gas, and waste water separated from oil or gas of which disposal is to be made by injection into a water disposal well. Thus, crude petroleum oil may be treated in the Well with sodium mercaptobenzothiazole to inhibit corrosion of the well equipment. Similarly, sodium mercaptobenzothiazole may be employed to inhibit corrosion in natural gas wells. Where water separated from oil or gas is to be injected into a water disposal well, the water may be treated with sodium mercaptobenzothiazole if the oil or gas fromwhich the water was separated was not treated previously in the Well or if additional treatment is desired. Crude petroleum oil or liquid petroleum products to be transported in pipe lines may also be treated in accordance with the invention. Frequently, liquid petroleum hydrocarbons, such as crude petroleum oils and liquid petroleum products, will not contain a free water phase at the time they enter the pipe line system. However, they may contain dissolved water and a free water phase will subsequently form as a result of condensation due to cooling by lowering of atmospheric temperature or by passage through sections of the pipe line at a lower than normal temperature, such as sections of the pipe line located under a lake or river. Where condensation occurs in a, liquid treated with sodium mercaptobenzothiazole, the sodium mercaptobenzothiazole will enter into solution in the water phase, thereby inhibiting corrosion at the points of the system in contact with the free water phase. This issparticularly advantageous for the inhibition=of corrosionat low pointsin the carrier pipe, as in valleys, dips, and the like, or in other spots of the system where free water will accumulate.
The concentration of sodium'mercaptobenzothiazole to be employed may be between about. 1
and 500 parts per million by weight of the liquid to be treated depending upon.the corrosivity. of the liquid. Within these limits, the concentration of sodium mercaptobenzothiazole to be employed will depend upon the amount of corrosive compounds in the liquid and the extent to which corrosion is to be inhibited. Generally, satisfactory results are obtainedwhere the sodium mercaptobenzothiazole. isxemployedain an amount between: aboutt50 andQlOQ' pants-per. million. by weight .ofwtheliquidi However; the exact concentrationto be employed in. each particular case to obtain.the'desireddegreeof inhibition of corrosion-:with minimum: concentration of sodium mercaptobenzothiazole ,may; bedetermined by immersing testpieces .of the same kind of ferrous metaliwhose'corrosion' is to be inhibited in samples: of the liquid to :be treated to which-have been added :varying amounts. of 'sodiummercaptobenzothiazole, andzcomparing-the extent of corrosion of;.eachrtestpieee-after a suitable immersiontime .with the amount of sodium' mercaptobenzothiazole in the samples of liquid.
preparing thesolution; However, saline waters.
mayalso be employed althoughtheir use is to be avoided since salt in-large concentra-tions :causes some degree of: precipitation ofthe sodium mercaptobenzothiazole; In this. connection, where the aliquidto betreatedcontains. salt. water, it is desirable to-employ'larger'.conoentrations of sodium mercaptobenzothiazole than'would be employed. if the liquid contained non-saline water.
Where corrosion:incan'oilwellis to be inhibited, the'sodium mercaptobenzothiazole may be intro duced into the wellbetween-the'tubing and the casing.v Gas-Wells may be similarly treated; the sodium-mercaptobenzothiazole admixingwith the water at the bottom of the well and inhibiting corrosion of ferrous metal equipment of the well contactedby th water lifted upwardly by the flow of gas. Crude-oil or liquid petroleum-products :to-be transported inapipe line system may betreated by adding .sodium mercaptobenzothiazole thereto-prior.- to-or at thetime of entering the :pipe line-system or may be-added subsequent toentering the pipeline systemibyinjecting into the pipelinesystem at a desired point or points. Waste wateninjected .into water disposal .wells may @be:treatedbyadmixing the sodium mercaptobenzothiazole therewith prior--to injection of. the .water intothe disposal well. If thecrude oilor. gas .fromwhich the wateris separatedhas been previously treated. with. sodium. mercaptobenzothiazole. the .watermay ,-contain,.-suflicient with sodium; mercaptobenzothiazole 4 sodium mercaptobenzothiazole to inhibit corrosion and no further treatment will be necessary. However, if insufficient sodium mercaptobenzothiazole is contained in the water, an additional amount may be added.
Thefollowing examples will. be illustrative of the-results to be obtained by the/process of the invention.
Example I In an oilnwell in the Brownfield District in Texas producing on the average 38 barrels of crude oil and 5 barrels of water per day, the ferrous: metal equipment in contact with the produced well liquidsi was being corroded at a rate of 0.0015 inch of penetration per year. This well was treatedbypumping sodium mercaptobenzothiazole in water solution between the tubing and the casing in amounts such that the concentration of sodium mercaptobenzothiazole in the total well liquids was 100 parts per million by weight." Thetreatment-was-continued for six months. During the first three months of 1 treatment the corrosion rate was reduced to'0.0005 inch'of penetration per'yean'a-decrease of 67 per cent, and during the second three-months of treatment the corrosion rate was'reduced to 0.0001 inch of-penetration-per=year-,- a decrease of 93 percent.
Example II Inanother wellin the same district producing on the average 38barrels of. crude oil and28 barrelsof. .water per day,,. the corrosion rate was 0.0078 inch.of..penetration.per year. Treatment in the amount of .10 parts .per millionv by weight of the totalwell liquidsswas. instituted and continued for two months. The corrosion rate was reduced to 0.0037 inch of. penetration per year, a decrease of. 53. percent. Thereafter, the concentration of sodium. mercaptobenzothiazole was increased to 100 parts per millionby weight .of the'total well liquidsand continued fora period of four months. The corrosionrate .was. reduced to 0.0023 .inch of penetration per. year, a decrease .of. 69 percent.
Having-.thusdescribed my invention,.it will be understood that suchidescriptionhas been given byway ,of illustration. and example only and not by way of limitation, reference for the latter purpose being. had to the appended claims.
I claim:
1. The .process for. inhibiting -corrosion of ferroussmetal in contact with a .liquidc comprising water,.said.water prior, to contact with said ferrousmetal having beenin contact with petroleum hydrocarbon andasaresult of. said contact with said. petroleum. hydrocarbon having extracted f rjomsaid .petroleum hydrocarbon. a Water-soluble compoundcorrosive to said. ferrous metal, which process comprises admixing with said liquid prior to contact with said ferrous. metal as the sole corrosion inhibiting agent. sodium mercaptobenzothiazolein corrosion. inhibiting amount.
2. The process of-claiinl wherein saidsodium mercaptobenzothiazole is admixed .withsaid liquidin anamount between about 1 and500 parts permilli'onrby weightof. said-liquid.
3... The process of. .claiml wherein said sodium mercaptobenzothiazole is admixedwi-th saidliquid .in an amountbetween about 50 and 100 parts per. million byweight of said liquid.
,4. The processfor inhibitingcorrosion of ferrous metalin a: petroleum-hydrocarbon well in contact with a. petroleum. hydrocarbon-well fluid containing water, saidwaterprior to contact with said ferrous metal having extracted from said petroleum hydrocarbon well fluid a water-soluble compound corrosive to said ferrous metal, which process comprises introducing into said well and admixing therein with said petroleum hydrocarbon well fiuid prior to contact of said petroleum hydrocarbon well fluid with said ferrous metal as the sole corrosion inhibiting agent sodium mercaptobenzothiazole in corrosion inhibiting amount.
5. The process for inhibiting corrosion of ferrous metal in a petroleum gas well in contact with petroleum gas admixed With water produced concomitantly with said petroleum gas, said water prior to contact with said ferrous metal having extracted from said gas a water-soluble compound corrosive to said ferrous metal, which process comprises introducing into said well and admixing therein with said water as the sole corrosion inhibiting agent sodium mercaptobenzothiazole in corrosion inhibiting amount.
6. The process for inhibiting internal corrosion in a ferrous metal pipe line transporting liquid petroleum hydrocarbons containing water, said water having extracted from petroleum hydrocarbons a water-soluble compound corrosive to said ferrous metal, which process comprises admixing With said liquid petroleum hydrocarbons as the sole corrosion inhibiting agent sodium mercaptobenzothiazole in corrosion inhibiting amount.
7. The process for inhibiting corrosion of ferrous metal in a water disposal well in contact with water separated from petroleum hydrocarbons, said water as a result of said contact with said petroleum hydrocarbons having extracted from said petroleum hydrocarbons a water-soluble compound corrosive to said ferrous metal, which process comprises admixing with said water prior to contact with said ferrous metal as the sole corrosion inhibiting agent sodium mercaptobenzothiazole in corrosion inhibiting amount.
References Cited in the file of this patent UNITED STATES PATENTS
Claims (1)
1. THE PROCESS FOR INHIBITING CORROSION OF FERROUS METAL IN CONTACT WITH A LIQUID COMPRISING WATER, SAID WATER PRIOR TO CONTACT WITH SAID FERROUS METAL HAVING BEEN IN CONTACT WITH PETROLEUM HYDROCARBON AND AS A RESULT OF SAID CONTACT WITH SAID PETROLEUM HYDROCARBON HAVING EXTRACTED FROM SAID PETROLUEM HYDROCARBON A WATER-SOLUBLE COMPOUND CORROSIVE TO SAID FERROUS METAL, WHICH PROCESS COMPRISES ADMIXING WITH SAID LIQUID PRIOR TO CONTACT WITH SAID FERROUS METAL AS THE SOLE CORROSION INHIBITING AGENT SODIUM MERCAPTOBENZOTHIAZOLE IN CORROSION INHIBITING AMOUNT.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US221937A US2691631A (en) | 1951-04-19 | 1951-04-19 | Method of inhibiting corrosion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US221937A US2691631A (en) | 1951-04-19 | 1951-04-19 | Method of inhibiting corrosion |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2691631A true US2691631A (en) | 1954-10-12 |
Family
ID=22830050
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US221937A Expired - Lifetime US2691631A (en) | 1951-04-19 | 1951-04-19 | Method of inhibiting corrosion |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2691631A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2832735A (en) * | 1955-11-17 | 1958-04-29 | Cities Service Res & Dev Co | Method of inhibiting corrosion of metals |
| US2865856A (en) * | 1955-11-17 | 1958-12-23 | Cities Service Res & Dev Co | Method of inhibiting corrosion of metals |
| US2935474A (en) * | 1955-11-28 | 1960-05-03 | Visco Products Co | Process of inhibiting corrosion and corrosion inhibiting compositions |
| DE1111900B (en) * | 1958-09-20 | 1961-07-27 | Dr Eberhard Krietsch | High temperature resistant inhibitors to prevent hot water corrosion |
| US3087897A (en) * | 1956-06-20 | 1963-04-30 | Stedt | Process of making a corrosion inhibiting composition |
| US20150101240A1 (en) * | 2010-04-30 | 2015-04-16 | Instituto Mexicano Del Petroleo | Multifunctional composition base 1,3-oxazinan-6-ones with corrosion inhibition and heavy organic compounds inhibition and dispersants and obtaining process |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1797401A (en) * | 1931-03-24 | And herbert w | ||
| US2474603A (en) * | 1946-12-20 | 1949-06-28 | Standard Oil Dev Co | Inhibition of corrosion in wells |
-
1951
- 1951-04-19 US US221937A patent/US2691631A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1797401A (en) * | 1931-03-24 | And herbert w | ||
| US2474603A (en) * | 1946-12-20 | 1949-06-28 | Standard Oil Dev Co | Inhibition of corrosion in wells |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2832735A (en) * | 1955-11-17 | 1958-04-29 | Cities Service Res & Dev Co | Method of inhibiting corrosion of metals |
| US2865856A (en) * | 1955-11-17 | 1958-12-23 | Cities Service Res & Dev Co | Method of inhibiting corrosion of metals |
| US2935474A (en) * | 1955-11-28 | 1960-05-03 | Visco Products Co | Process of inhibiting corrosion and corrosion inhibiting compositions |
| US3087897A (en) * | 1956-06-20 | 1963-04-30 | Stedt | Process of making a corrosion inhibiting composition |
| DE1111900B (en) * | 1958-09-20 | 1961-07-27 | Dr Eberhard Krietsch | High temperature resistant inhibitors to prevent hot water corrosion |
| US20150101240A1 (en) * | 2010-04-30 | 2015-04-16 | Instituto Mexicano Del Petroleo | Multifunctional composition base 1,3-oxazinan-6-ones with corrosion inhibition and heavy organic compounds inhibition and dispersants and obtaining process |
| US9586915B2 (en) * | 2010-04-30 | 2017-03-07 | Instituto Mexicano Del Petroleo | Multifunctional composition base 1,3-oxazinan-6-ones with corrosion inhibition and heavy organic compounds inhibition and dispersants and obtaining process |
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