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US3514410A - Prevention of ferric ion corrosion using acid cleaning solution containing hydrogen sulfide and an aldehyde corrosion inhibitor - Google Patents

Prevention of ferric ion corrosion using acid cleaning solution containing hydrogen sulfide and an aldehyde corrosion inhibitor Download PDF

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US3514410A
US3514410A US656662A US3514410DA US3514410A US 3514410 A US3514410 A US 3514410A US 656662 A US656662 A US 656662A US 3514410D A US3514410D A US 3514410DA US 3514410 A US3514410 A US 3514410A
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aldehyde
hydrogen sulfide
corrosion
acid
inhibitor
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James P Engle
Bill R Keenry
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Halliburton Co
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    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • C23G1/04Cleaning or pickling metallic material with solutions or molten salts with acid solutions using inhibitors

Definitions

  • This patent relates to a method of treating ferrous metal surfaces to remove iron oxide encrustations which comprises contacting the surface with an aqueous solution comprising an acid, a hydrogen sulfide liberating material and an aldehyde-containing corrosion inhibitor.
  • Ferric oxide encrustations commonly known as rust, frequently form on ferrous metal surfaces.
  • Various methods of removing the ferric oxide encrustations have been devised, a common one being to contact the ferrous surface with an acid such as hydrochloric acid to thereby dissolve the ferric oxide and thus remove the rust encrustations from the surface.
  • an iron salt is formed, the specific ferric salt depending upon the acid used.
  • hydrochloric acid is used, ferric chloride is formed.
  • severe corrosion problems may be experienced during acid cleaning of ferrous surfaces.
  • Ferric chloride is formed as follows:
  • Ferric chloride is rapidly and quantitatively reduced to ferrous chloride by iron or copper in acid solutions.
  • the reduction of ferric chloride by iron is shown in the following equation:
  • this invention relates to a method of removing ferric oxide encrustations from metal surfaces.
  • ferric ion corrosion presents a severe problem.
  • ferric ion corrosion is almost entirely eliminated by incorporating into the cleaning acid solution a source of hydrogen sulfide andcacorromsjgn i nhibitor containingan aldehyde,.and ru'gferably containing It is thus ifi'object of the present invention to provide a method and composition for the treating of ferrous metal surfaces to remove iron oxide encrustations.
  • the present invention involves the process of rust removal from ferrous surfaces by treating with an acid.
  • the present process involves the use of a solution of acid which also contains, hydrogen sulfide or a hydrogen sulfide source and an aldehyde-containing corrosion inhibitor.
  • hydrogen sulfide is considered very corrosive to ferrous surfaces and great pains are taken to avoid contacting the ferrous surfaces with the hydrogen sulfide.
  • the hydrogen sulfide and aldehyde-containing corrosion inhibitor should be incorporated into the acid cleaning solution at the time it contacts the metal surface or very readily thereafter. Clearly, ferric ion corrosion will result if they are not added before ferric ions are formed.
  • the hydrogen sulfide may be added by any convenient method.
  • hydrogen sulfide gas may be bubbled into the hydrochloric acid solution prior to treatment or during treatment of the ferrous surface.
  • various materials which liberate hydrogen sulfide e.g., any acid soluble sulfide, may be used.
  • Ferrous sulfide will react in a hydrochloric acid solution to produce hydrogen sulfide.
  • thioacetamide will also react in a hydrochloric acid solution to produce hydrogen sulfide.
  • the hydrogen sulfide may be present as such or as a hydrogen sulfide source.
  • the invention will work satisfactorily with a hydrogen sulfide concentration over a fairly' large range. This, from about 0.1% to about 5% hydrogen sulfide may be present in the solution. In general, it is desired that the molar concentration of hydrogen sulfide be at least equal to the number of moles of ferric chloride produced during the acid treating operation. It can be seen that the hydrogen sulfide concentration will thus vary depending upon the amounts of ferric ion present. In general, a hy-.
  • the corrosion inhibitor may comprise an aldehyde alone, it is preferred that it comprise an aldehyde in combination with an acetylenic compound or a nitrogen containing compound.
  • the preferred inhibitor comprises an aldehyde and a material selected from the group consisting of a nitrogen containing organic compound, an acetylenic compound and mixtures thereof.
  • any aldehyde may be used in this invention.
  • suitable aldehydes include alkyl aldehydes, aryl aldehydes and alkylaryl aldehydes.
  • the aldehydes may be substituted with nondeleterious substituents such as a hyf
  • the aldehyde may droxyl group and may be saturated or unsaturated.
  • Suitable aldehydes include forrnaldehyde, benzaldehyde, butyraldehyde, B-hydroxy butyraldehyde (aldol), propionaldehyde, and glyoxal,
  • the aldehyde may be used alone or in a suitable solvent such as alcohol.
  • a convenient method of using formaldehyde is the use of a solution of formaldehyde in alcohol.
  • formaldehyde may be dissolved in an approximately equal amount of methanol.
  • Other alcohols such as ethyl alcohol, propyl alcohol, butyl alcohol, and isobutyl alcohol may also be used.
  • Solutions of formaldehyde in alcohol such as Methyl Formcel (formaldehyde in methanol) are readily available commercially from the Celanese Chemical Company.
  • Another convenient form of formaldehyde is paraformaldehyde, a solid polymer of formaldehyde.
  • the nitrogen bearing organic compounds of this invention include amines, quaternary ammonium salts, amides, imines, imidazolines, etc.
  • the amines may be primary, secondary or tertiary and contain alkyl, aryl, or alkaryl substituents. Suitable amines include mono, di and trialkyl amines and N-heterocyclic amines.
  • amines which are well-known in the corrosion inhibitor art may be used in this invention.
  • examples of such amines are rosin amine, dehydroabiethylamine, pyridine and alkyl pryidines such as alkyl pyridines having from 1 to 5 nuclear alkyl substituents per pyridine moiety,
  • the concentration of aldehyde and the concentration of the organic nitrogen compound or acetylenic compound are not interdependent and thus significant improvement in corrosion protection can be obtained by varying the concentration of one of the components in the corrosive medium without varying that of the other.
  • the aldehyde concentration in the corrosive medium may vary from about 0.003 to 10%.
  • concentration of the nitrogen bearing organic inhibitor in aqueous acid solution may vary from about 0.05 to 10% while the acetylenic inhibitor concentration will normally vary between 0.05 and 10% by volume.
  • the aldehyde and inhibitor component may be premixed before being added to a corrosive environment. However, if desired, they may also be added separately. Thus, an inhibitor component such as a nitrogen bearing organic compound may first be added to a corrosiveenvironment and later the aldehyde may be added. However, to obtain the most effective protection, it is generally desirable to add the aldehyde at the same time as the other components.
  • a particularly efifective inhibitor comprises a mixture of an acetylenic alcohol, a nitrogen compound, and an aldehyde dissolved in an alcohol. On a basis of a volume 100% this composition is comprised as foilows:
  • alkyl substituents having from 1 to 12 carbon atoms P e t and preferably those having an average of 6 carbon Acgtylenic compound 41-92 atoms per pyridine moiety, such as a mixture of high- Nitrogen or ammonia base compound 3 9 boiling tertiary-nitrogen-heterocyclic compounds such as HAP (High Alkyl Pyridines), Reilly 10-20 base and Alkyl Pyridines HB, primary alkyl amines containing 12 to 14 carbon atoms known commercially as Primene 81 R and sold by Rohn and Haas, aniline, etc.
  • HAP High Alkyl Pyridines
  • Reilly 10-20 base and Alkyl Pyridines HB primary alkyl amines containing 12 to 14 carbon atoms known commercially as Primene 81 R and sold by Rohn and Haas, aniline, etc.
  • acetylenic compounds of this invention may be alkyl and aryl hydrocarbons. They may be substituted such as with hydroxyl groups and other nondeleterious substituents, e.g., acetylenic amines, ketones, aldehydes, halogens, esters, acids, etc.
  • acetylenic compounds include hexynol, dimethyl hexynol, dimethyl hexynediol, diethyl hexynediol, dimethyl octynediol, methyl butynol, methyl pentynol, ethynyl cyclohexanol, 2-ethyl hexynol, phenyl butynol, dodecyclaminopropyne and ditertiary acetylenic glycol.
  • Acetylenic sulfides ha ing the general formula HCECR-SR-CECH can also be employed in the present invention in lieu of the acetylenic alcohol.
  • examples of these are dipropargyl sulfide, bis(1-methyl- 2-propynyl) sulfide and bis(2-ethylnyl-2-propyl) sulfide.
  • Another efiective composition is the combination of an aldehyde, e.g., Methyl Formcel, with a composition comprising 41%92% of an acetylenic compound, 3%-9% of a nitrogen compound and 5 %-50% of a nonacetylenic alcohol.
  • Methyl Formcel contains methanol, 'it also adds to the nonacetylenic alcohol concentration.
  • Suitable nonacetylenic alcohols include those having the general remuianou, wherein R is either an group.
  • Some examples of these alkyl group or a ketone alcohols are diacetone alcohol, normal propanol, isopropanol, ethanol, methanol, ethylene glycol, diethylene glycol, propylene glycol, glycol, and 1,5-pentanediol.
  • the amount of inhibitor used may vary from about 0.1% to about 10%. However, it has been found that a concentration of about 0.1% to 1% will normally be sufiicient for most uses. Of course, the amount of inhibitor will depend at least in part on the amount of hydrogen sulfide present, larger inhibitor concentrations being required for larger sulfide concentrations.
  • the acid used in removing the ferric oxide encrustations should be a strong mineral acid capable of rapidly removing the rust. In general, hydrochloric acid is used.
  • EXAMPLE I base solution to ascertain the exact acid concentration.
  • the various acid solutions were prepared in advance in dipropylene glycol, hexylene sufi'icient quantities to complete an entire series of tests with the same batch of acid.
  • Corrosion coupons of the metal tested were ordered bearing organic compound alone, with the acetylenic compound alone, or with a combination of the two.
  • krelative proportionof aldehyde and inhibitor may vary in sufficient quantities to complete a series of tests on the same batch of coupons.
  • the coupons were cleaned as follows: pickled in an uninhibited HCl acid solution for 10 minutes, neutralized in a 10% solution of sodium bicarbonate, scrubbed by hand with a fine wire brush and a detergent containing a pumice, rinsed, dipped in acetone to remove the excess water and then dipped in alcohol and allowed to dry. They were then Weighed to the nearest milligram and stored in a desiccator until time for use.
  • the acid solution was poured into glass bottles in sufficient quantity to approximate the specific acid volume to coupon surface area ratio that was desired.
  • the quantity of acid used was dependent upon the surface area of the coupon to be tested. In most of the tests, a 25 cc./in. acid volume to coupon surface area ratio was used.
  • the inhibitor was added with a hypodermic syringe and the resulting solution was stirred with a glass rod.
  • the inhibited acid solution was then placed in a water bath which had been set at a predetermined temperature and allowed to preheat for minutes,,after which time, the coupons were placed in the preheated inhibited acid solutions.
  • the coupons were left in the acid solutions for the specified test time, then removed, neutralized, recleaned, rinsed, dipped in acetone then alcohol, allowed to dry, then reweighed.
  • the loss in weight in grams was multiplied times a calculated factor to convert the loss in weight to lbs./ft. /24 hrs.
  • the factor was calculated as follows:
  • the inhibitors used in this invention were Rodine 213, an inhibitor containing the reaction product of rosin amine, formaldehyde and a ketone, and two inhibitors designated as Blend 1 and Blend 2, the compositions of which are set forth 'below.
  • FeC a Do 5% B01--. 0.5% FeS+l.0% 0.3 0.032
  • the ferrous containing metal corrodes at a rapid rate in the presence of hydrochloric acid and ferric chloride even in the presence of the inhibitor.
  • the corrosion rate is reduced to a very low level:
  • any method of treatment of a ferrous surface with hydrochloric acid or any acid which will produce a ferric ion capable of resulting in ferric ion corrosion may be used.
  • concentrations of hydrogen sulfide and inhibitor may be used depending upon the conditions of concentration, temperature, etc., under which the treatment of the ferrous metal occurs.
  • a method of treating metal ferrous surfaces to remove iron oxide encrustations comprising treating the surface with an aqueous solution comprising an hydrochloric acid, hydrogen sulfide and an aldehyde-containing corrosion inhibitor.
  • the inhibitor is a composition comprising an aldehyde and a material selected from the group consistmg of nitrogen bearing organic compounds, acetylenic compounds and mixtures thereof.
  • aldehyde is selected from the group consisting of formaldehyde, crotonaldehyde, benzaldehyde, butyraldehyde, propionaldehyde, glyoxal, aldol and mixtures thereof.
  • concentration of said inhibitor is from about 0.1% to 10%.
  • a method of treating metal ferrous surfaces to remove iron oxide encrustations comprising treating the 8 surface with an aqueous solution comprising an hydrochloric acid, material capable of producing hydrogen sulfide in acid solution and an aldehyde-containing corrosion inhibitor
  • an aqueous solution comprising an hydrochloric acid, material capable of producing hydrogen sulfide in acid solution and an aldehyde-containing corrosion inhibitor

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Description

08? armor I 3,514,410 Patented May 26, 1970 3,514,410 PREVENTION OF FERRIC ION CORROSION USING ACID CLEANING SOLUTION CONTAINING HY- DROGEN SULFIDE AND AN ALDEI-IYDE COR- ROSION INHIBITOR James P. Engle and Bill R. Keeney, Duncan, Okla., assignors to Halliburton Company, Duncan, kla., a corporation of Delaware No Drawing. Filed July 28, 1967, Ser. No. 656,662 Int. Cl. C02b 5/02, 5/06 US. Cl. 252-87 13 Claims ABSTRACT OF THE DISCLOSURE This patent relates to a method of treating ferrous metal surfaces to remove iron oxide encrustations which comprises contacting the surface with an aqueous solution comprising an acid, a hydrogen sulfide liberating material and an aldehyde-containing corrosion inhibitor.
BACKGROUND OF THE INVENTION Ferric oxide encrustations, commonly known as rust, frequently form on ferrous metal surfaces. Various methods of removing the ferric oxide encrustations have been devised, a common one being to contact the ferrous surface with an acid such as hydrochloric acid to thereby dissolve the ferric oxide and thus remove the rust encrustations from the surface. As a result of this operation, an iron salt is formed, the specific ferric salt depending upon the acid used. When hydrochloric acid is used, ferric chloride is formed. As a result of the ferric ion formation, severe corrosion problems may be experienced during acid cleaning of ferrous surfaces.
Ferric chloride is formed as follows:
Ferric chloride is rapidly and quantitatively reduced to ferrous chloride by iron or copper in acid solutions. The reduction of ferric chloride by iron is shown in the following equation:
E=1.2l volts This stoichiometric reaction is known as ferric ion corro= sion. It is because ferric chloride attacks copper that it is used as an etchant in preparing printed circuits in electronic equipment. In chemical cleaning, ferric chloride produces corrosion of the ferrous equipment being cleaned as well as pumps and transfer lines to and from the equipment. It can be calculated that for every thousand pounds of ferric chloride formed there will be an attendant metal loss of 173 pounds of steel. Of course, it is customary to carry out the acid cleaning of ferrous surfaces in the presence of a corrosion inhibitor to prevent the corrosion which would normally occur in the presence of an acid. However, these ordinary inhibitors have been of no value in preventing ferric ion corrosion.
SUMMARY Briefly, this invention relates to a method of removing ferric oxide encrustations from metal surfaces. In the normal cleaning methods involving, e.g., hydrochloric acid, ferric ion corrosion presents a severe problem. According to thisinvention, ferric ion corrosion is almost entirely eliminated by incorporating into the cleaning acid solution a source of hydrogen sulfide andcacorromsjgn i nhibitor containingan aldehyde,.and ru'gferably containing It is thus ifi'object of the present invention to provide a method and composition for the treating of ferrous metal surfaces to remove iron oxide encrustations.
It is a further object of this invention to provide a DESCRIPTION OF PREFERRED EMBODIMENTS In general, the present invention involves the process of rust removal from ferrous surfaces by treating with an acid. However, rather than merely treating with an aqueous acid, the present process involves the use of a solution of acid which also contains, hydrogen sulfide or a hydrogen sulfide source and an aldehyde-containing corrosion inhibitor.
Normally, hydrogen sulfide is considered very corrosive to ferrous surfaces and great pains are taken to avoid contacting the ferrous surfaces with the hydrogen sulfide. However, we have surprisingly found that in the presence of an acid, hydrogen sulfide and a corrosion inhibitor containing an aldehyde, the hydrogen sulfide has no deleterious effects and the rate of corrosion due to the ferric ion is greatly reduced.
The hydrogen sulfide and aldehyde-containing corrosion inhibitor should be incorporated into the acid cleaning solution at the time it contacts the metal surface or very readily thereafter. Clearly, ferric ion corrosion will result if they are not added before ferric ions are formed.
The hydrogen sulfide may be added by any convenient method. Thus, hydrogen sulfide gas may be bubbled into the hydrochloric acid solution prior to treatment or during treatment of the ferrous surface. Additionally, various materials which liberate hydrogen sulfide, e.g., any acid soluble sulfide, may be used. Ferrous sulfide will react in a hydrochloric acid solution to produce hydrogen sulfide. Additionally, thioacetamide will also react in a hydrochloric acid solution to produce hydrogen sulfide. Thus, the hydrogen sulfide may be present as such or as a hydrogen sulfide source.
The invention will work satisfactorily with a hydrogen sulfide concentration over a fairly' large range. This, from about 0.1% to about 5% hydrogen sulfide may be present in the solution. In general, it is desired that the molar concentration of hydrogen sulfide be at least equal to the number of moles of ferric chloride produced during the acid treating operation. It can be seen that the hydrogen sulfide concentration will thus vary depending upon the amounts of ferric ion present. In general, a hy-.
by weight reinhibitor which contains an aldehyde will result in a decreased rate of corrosion rather than an increased rate of corrosion as is the case when hydrogen sulfide alone is present. Although the corrosion inhibitor may comprise an aldehyde alone, it is preferred that it comprise an aldehyde in combination with an acetylenic compound or a nitrogen containing compound.
The preferred inhibitor comprises an aldehyde and a material selected from the group consisting of a nitrogen containing organic compound, an acetylenic compound and mixtures thereof.
In general, any aldehyde may be used in this invention. Thus, suitable aldehydes include alkyl aldehydes, aryl aldehydes and alkylaryl aldehydes. The aldehydes may be substituted with nondeleterious substituents such as a hyf The aldehyde may droxyl group and may be saturated or unsaturated. Suitable aldehydes include forrnaldehyde, benzaldehyde, butyraldehyde, B-hydroxy butyraldehyde (aldol), propionaldehyde, and glyoxal, The aldehyde may be used alone or in a suitable solvent such as alcohol.
A convenient method of using formaldehyde is the use of a solution of formaldehyde in alcohol. For example, formaldehyde may be dissolved in an approximately equal amount of methanol. Other alcohols such as ethyl alcohol, propyl alcohol, butyl alcohol, and isobutyl alcohol may also be used. Solutions of formaldehyde in alcohol such as Methyl Formcel (formaldehyde in methanol) are readily available commercially from the Celanese Chemical Company. Another convenient form of formaldehyde is paraformaldehyde, a solid polymer of formaldehyde.
The nitrogen bearing organic compounds of this invention include amines, quaternary ammonium salts, amides, imines, imidazolines, etc. The amines may be primary, secondary or tertiary and contain alkyl, aryl, or alkaryl substituents. Suitable amines include mono, di and trialkyl amines and N-heterocyclic amines. This includes such amines as ethylamine, diethylamine, triethylamine, proplyamine, dipropylamine, tripropylamine, mono, di, and tributylamine, mono, di and tripentylamine, mono, di and trihexylamine and isomers of these such as isopropylamine, tertiarybutylamine, aniline, etc. Any of the amines which are well-known in the corrosion inhibitor art may be used in this invention. Examples of such amines are rosin amine, dehydroabiethylamine, pyridine and alkyl pryidines such as alkyl pyridines having from 1 to 5 nuclear alkyl substituents per pyridine moiety,
over a wide range. Furthermore, it has been found that the concentration of aldehyde and the concentration of the organic nitrogen compound or acetylenic compound are not interdependent and thus significant improvement in corrosion protection can be obtained by varying the concentration of one of the components in the corrosive medium without varying that of the other. In general, the aldehyde concentration in the corrosive medium may vary from about 0.003 to 10%. However, lower or higher concentrations will still be effective although the effect of a lower concentration will be small and the amount of improvement obtained by adding more than 10% will generally be negligible. The concentration of the nitrogen bearing organic inhibitor in aqueous acid solution may vary from about 0.05 to 10% while the acetylenic inhibitor concentration will normally vary between 0.05 and 10% by volume. Once again, concentrations outside this range may be used, the exact concentration often being dictated by the economics of the situation.
The aldehyde and inhibitor component may be premixed before being added to a corrosive environment. However, if desired, they may also be added separately. Thus, an inhibitor component such as a nitrogen bearing organic compound may first be added to a corrosiveenvironment and later the aldehyde may be added. However, to obtain the most effective protection, it is generally desirable to add the aldehyde at the same time as the other components.
A particularly efifective inhibitor comprises a mixture of an acetylenic alcohol, a nitrogen compound, and an aldehyde dissolved in an alcohol. On a basis of a volume 100% this composition is comprised as foilows:
said alkyl substituents having from 1 to 12 carbon atoms P e t and preferably those having an average of 6 carbon Acgtylenic compound 41-92 atoms per pyridine moiety, such as a mixture of high- Nitrogen or ammonia base compound 3 9 boiling tertiary-nitrogen-heterocyclic compounds such as HAP (High Alkyl Pyridines), Reilly 10-20 base and Alkyl Pyridines HB, primary alkyl amines containing 12 to 14 carbon atoms known commercially as Primene 81 R and sold by Rohn and Haas, aniline, etc.
1 The acetylenic compounds of this invention may be alkyl and aryl hydrocarbons. They may be substituted such as with hydroxyl groups and other nondeleterious substituents, e.g., acetylenic amines, ketones, aldehydes, halogens, esters, acids, etc. Examples of suitable acetylenic compounds include hexynol, dimethyl hexynol, dimethyl hexynediol, diethyl hexynediol, dimethyl octynediol, methyl butynol, methyl pentynol, ethynyl cyclohexanol, 2-ethyl hexynol, phenyl butynol, dodecyclaminopropyne and ditertiary acetylenic glycol.
Other acetylenic compounds which can be employed in accordance with the present invention are for example methylbutynol, ethyl octynol, methylpentynol, butynediol, l-ethynylcyclohexanol, 3-methyl-l-nonyn-3-ol, 2-methyl- S-butyn-Z-ol, also l-propyn-3-ol, 1-butyn-3-ol, l-pentyn- 3-01, l-heptyn-B-ol, 1-octyn-3-ol, 1-nonyl-3-ol, bdecyn- 3 o1, l-(2,4,6-trimethyl-3cyclohexenyl)3-propyne-1-ol, and in general acetylenic compounds having the general formula wherein R is H, alkyl, phenyl, substituted phenyl or bydroxyalltyl radical, and the alpha Rs may be joined together to form a cyclohexyl ring.
Acetylenic sulfides ha ing the general formula HCECR-SR-CECH can also be employed in the present invention in lieu of the acetylenic alcohol. Examples of these are dipropargyl sulfide, bis(1-methyl- 2-propynyl) sulfide and bis(2-ethylnyl-2-propyl) sulfide. be combined with either the nitrogen Aldehyde Another efiective composition is the combination of an aldehyde, e.g., Methyl Formcel, with a composition comprising 41%92% of an acetylenic compound, 3%-9% of a nitrogen compound and 5 %-50% of a nonacetylenic alcohol. Since Methyl Formcel contains methanol, 'it also adds to the nonacetylenic alcohol concentration. Suitable nonacetylenic alcohols include those having the general remuianou, wherein R is either an group. Some examples of these alkyl group or a ketone alcohols are diacetone alcohol, normal propanol, isopropanol, ethanol, methanol, ethylene glycol, diethylene glycol, propylene glycol, glycol, and 1,5-pentanediol.
The amount of inhibitor used may vary from about 0.1% to about 10%. However, it has been found that a concentration of about 0.1% to 1% will normally be sufiicient for most uses. Of course, the amount of inhibitor will depend at least in part on the amount of hydrogen sulfide present, larger inhibitor concentrations being required for larger sulfide concentrations.
The acid used in removing the ferric oxide encrustations should be a strong mineral acid capable of rapidly removing the rust. In general, hydrochloric acid is used.
The invention can be more fully understood by reference to the following examples.
EXAMPLE I base solution to ascertain the exact acid concentration. The various acid solutions were prepared in advance in dipropylene glycol, hexylene sufi'icient quantities to complete an entire series of tests with the same batch of acid.
Corrosion coupons of the metal tested were ordered bearing organic compound alone, with the acetylenic compound alone, or with a combination of the two. The
krelative proportionof aldehyde and inhibitor may vary in sufficient quantities to complete a series of tests on the same batch of coupons. The coupons were cleaned as follows: pickled in an uninhibited HCl acid solution for 10 minutes, neutralized in a 10% solution of sodium bicarbonate, scrubbed by hand with a fine wire brush and a detergent containing a pumice, rinsed, dipped in acetone to remove the excess water and then dipped in alcohol and allowed to dry. They were then Weighed to the nearest milligram and stored in a desiccator until time for use.
The acid solution was poured into glass bottles in sufficient quantity to approximate the specific acid volume to coupon surface area ratio that was desired. The quantity of acid used was dependent upon the surface area of the coupon to be tested. In most of the tests, a 25 cc./in. acid volume to coupon surface area ratio was used.
After the desired amount of acid was poured into the bottles, the inhibitor was added with a hypodermic syringe and the resulting solution was stirred with a glass rod. The inhibited acid solution was then placed in a water bath which had been set at a predetermined temperature and allowed to preheat for minutes,,after which time, the coupons were placed in the preheated inhibited acid solutions. The coupons were left in the acid solutions for the specified test time, then removed, neutralized, recleaned, rinsed, dipped in acetone then alcohol, allowed to dry, then reweighed.
The loss in weight in grams was multiplied times a calculated factor to convert the loss in weight to lbs./ft. /24 hrs. The factor was calculated as follows:
ftz =Factor 1 day 2 454gb Surface Area of Coupon 1n X hrs Example: Test time, 6 hours, Surface Area of Coupon,
2 m then 454 4.0 6/24 454 4.0
The inhibitors used in this invention were Rodine 213, an inhibitor containing the reaction product of rosin amine, formaldehyde and a ketone, and two inhibitors designated as Blend 1 and Blend 2, the compositions of which are set forth 'below.
BLEND l The tests were conducted at 175 F. for 6 hours in 10% hydrochloric acid. The ferrous metal tested was A151- 1010 carbon steel with an acid volume to surface area ratio of 22 cc./in. The results are set forth in Table 1 below.
TABLE I Corrosion Concentra- Rate in lbs Inhibitor tlon, percent Contaminant it. /day Blend 1 0.3 No 0. 002 0.3 1.0% FeCla 0.037 0.3 l.0% MGM-1.0% FeB.. 0.074 Blend 2 0.3 No 0.003 0.3 1.0% FeCl; 0.039 Do 0.3 1.0% FeCh+ 0.011 Rodine-213 0.3 None.. 0.006 D 0.3 1. FeCln. 0.043 Do 0.3 1.0% F8C l+1.0% FeB.. 0.02s
6 EXAMPLE 11 The inhibitor contained 3.4 parts of Methyl Formcel and 6.6 parts of Blend 1 set forth in Example I.
The results are set forth in Table 2.
TABLE 2 Inkibitor Corrosion concentrarate in 1bs./
Metal Type Corrodent Additive tlon, percent Itfi/Zlhours 416 SS 5% H01.-. None 0.2 0.421 416 SS 5% H01.-- 0.5% Fes 0. 2 0. 008 416 SS 5% 1101..- 1.0% FeCl: 0. 2 0. 814 416 SS 5% HCL 0.15 %CI]ieS+1.0% 0.2 0.013
e a 5% H01--. None. 0.3 0.089 5% E01... 1.0% FeCla 0.3 0.099 0.4 0. 019 0.4 0. 0H 0.2 0. 87 0. 2 0. 058 0.2 0. 90 0. 2 0. 10
FeC a. Do 5% B01--. 0.5% FeS+l.0% 0.3 0.032
F8013, 5 H01 0.3 0. 176 5% HCl... 1.0% F60 0. 3 0.185 5% HCl-.- N 0. 4 0. 11.8 5% HCl... 1.0% FoCl; 0.4 0. 112
It can be seen from the foregoing examples that the ferrous containing metal corrodes at a rapid rate in the presence of hydrochloric acid and ferric chloride even in the presence of the inhibitor. However, in the presence of both the aldehyde-containing inhibitor and the hydrogen sulfide or hydrogen sulfide source, the corrosion rate is reduced to a very low level:
It should be understood that the foregoing examples are merely illustrative and should not be considered to limit the scope of the invention. Indeed, the scope of the invention is to be limited only by the legal scope of the appended claims.
It can readily be seen to one skilled in the art that many variations in the present invention may be used. In general, any method of treatment of a ferrous surface with hydrochloric acid or any acid which will produce a ferric ion capable of resulting in ferric ion corrosion may be used. Furthermore, any suitable method of providing hy= drogen sulfide and an aldehyde-containing inhibitor may 'be used. In addition, it can readily be seen that wide variations in the concentrations of hydrogen sulfide and inhibitor may be used depending upon the conditions of concentration, temperature, etc., under which the treatment of the ferrous metal occurs.
We claim:
1. A method of treating metal ferrous surfaces to remove iron oxide encrustations comprising treating the surface with an aqueous solution comprising an hydrochloric acid, hydrogen sulfide and an aldehyde-containing corrosion inhibitor.
2. The method of claim 1 wherein the hydrogen sulfide is obtained from ferrous sulfide provided in said solution.
3. The method of claim 1 wherein the hydrogen sulfide is obtained from thioacetamide provided in said solution.
4. The method of claim 1 wherein hydrogen sulfide gas is bubbled through said solution.
5. The method of claim 1 wherein the inhibitor is a composition comprising an aldehyde and a material selected from the group consistmg of nitrogen bearing organic compounds, acetylenic compounds and mixtures thereof.
6. The method of claim 5 wherein the nitrogen hearing compound is an amine.
7. The method of claim 5 wherein the acetylenic com pound is propargyl alcohol.
8. The method of claim 6 wherein the aldehyde is selected from the group consisting of formaldehyde, crotonaldehyde, benzaldehyde, butyraldehyde, propionaldehyde, glyoxal, aldol and mixtures thereof.
9. The method of claim 8 wherein the aldehyde is formaldehyde.
10. The method of claim 9 wherein the aldehyde is present in the form of an alcohol solution.
11. The method of claim 10 wherein the concentration of said inhibitor is from about 0.1% to 10%.
12. The process of claim 10 wherein the hydrogen sulfide concentration is from about 0.1% to 5% by weight.
13. A method of treating metal ferrous surfaces to remove iron oxide encrustations comprising treating the 8 surface with an aqueous solution comprising an hydrochloric acid, material capable of producing hydrogen sulfide in acid solution and an aldehyde-containing corrosion inhibitor References Cited UNITED STATES PATENTS 3,049,496 8/1962 Monroe 252-446 JOHN T. GOOLKASIAN, Primary Examiner M. E. McCAMISH, Assistant Examiner U.S. c1 X.R.
US656662A 1967-07-28 1967-07-28 Prevention of ferric ion corrosion using acid cleaning solution containing hydrogen sulfide and an aldehyde corrosion inhibitor Expired - Lifetime US3514410A (en)

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US3779935A (en) * 1971-07-12 1973-12-18 Exxon Research Engineering Co Inhibition of corrosion
US3981740A (en) * 1974-04-19 1976-09-21 Universal Oil Products Company Method for the removal and inhibition of metal scale formation in a hydrocarbon processing unit
EP0012478A2 (en) * 1978-12-06 1980-06-25 The Dow Chemical Company Method for removing sulfide-containing scale from metal surfaces
EP0139567A2 (en) * 1983-09-30 1985-05-02 Pumptech N.V. Method and composition for inhibiting corrosion
US4680127A (en) * 1985-12-13 1987-07-14 Betz Laboratories, Inc. Method of scavenging hydrogen sulfide
US5085842A (en) * 1990-01-25 1992-02-04 Hoechst Aktiengesellschaft Process for scavenging hydrogen sulfide using glyoxal
US5152916A (en) * 1989-08-23 1992-10-06 Hoechst Aktiengesellschaft Aqueous aldehyde solutions for trapping hydrogen sulfide in natural gas and crude oil producing plants
US5225103A (en) * 1989-08-23 1993-07-06 Hoechst Aktiengesellschaft Aqueous aldehyde solutions for trapping hydrogen sulfide in natural gas and crude oil producing plants
US5854180A (en) * 1998-03-24 1998-12-29 Clearwater, Inc. Environmentally improved acid corrosion inhibitor
US6666975B1 (en) 2002-10-04 2003-12-23 Ge Betz, Inc. Method of reducing hydrogen sulfide odor emissions from an aqueous medium
EP1624089A1 (en) 2004-07-08 2006-02-08 General Electric Company Method of preventing hydrogen sulfide odor generation in an aqueous medium
US20060073112A1 (en) * 2004-10-01 2006-04-06 Whitekettle Wilson K Method of preventing hydrogen sulfide odor generation in an aqueous medium
US20070131625A1 (en) * 2005-12-12 2007-06-14 General Electric Company Methods of inhibiting biogenic sulfide formation in aqueous systems
US20090068059A1 (en) * 2007-09-12 2009-03-12 Whitekettle Wilson K Method of preventing hydrogen sulfide odor generation in an aqueous medium
US20110100630A1 (en) * 2009-11-02 2011-05-05 Baker Hughes Incorporated Method of Mitigating Corrosion Rate of Oilfield Tubular Goods
US20130112106A1 (en) * 2011-11-08 2013-05-09 Mark A. Malwitz Environmentally friendly corrosion inhibitor
WO2015142633A1 (en) 2014-03-18 2015-09-24 Baker Hughes Incorporated Dimercaptothiadiazoles to prevent corrosion of mild steel by acid gases in oil and gas products
WO2016118400A1 (en) 2015-01-22 2016-07-28 Baker Hughes Incorporated Use of hydroxyacid to reduce the localized corrosion potential of low dose hydrate inhibitors
US20170175275A1 (en) * 2013-09-23 2017-06-22 Agienic, Inc. Compositions For Use In Corrosion Protection
US9732430B2 (en) 2013-10-24 2017-08-15 Baker Hughes Incorporated Chemical inhibition of pitting corrosion in methanolic solutions containing an organic halide
US10400339B2 (en) * 2013-09-23 2019-09-03 Agienic, Inc. Low water solubility compositions for use in corrosion protection
US11034921B2 (en) 2018-05-16 2021-06-15 Adam Mason PRINCE Method, kit, and composition for corrosion removal
WO2022178251A1 (en) 2021-02-19 2022-08-25 Nissan Chemical America Corporation Use of silica nanoparticles with glyoxal for h2s scavenging

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US3049496A (en) * 1959-04-30 1962-08-14 Dow Chemical Co Propargyl compounds as corrosion inhibitors

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US3049496A (en) * 1959-04-30 1962-08-14 Dow Chemical Co Propargyl compounds as corrosion inhibitors

Cited By (31)

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Publication number Priority date Publication date Assignee Title
US3779935A (en) * 1971-07-12 1973-12-18 Exxon Research Engineering Co Inhibition of corrosion
US3981740A (en) * 1974-04-19 1976-09-21 Universal Oil Products Company Method for the removal and inhibition of metal scale formation in a hydrocarbon processing unit
EP0012478A2 (en) * 1978-12-06 1980-06-25 The Dow Chemical Company Method for removing sulfide-containing scale from metal surfaces
US4220550A (en) * 1978-12-06 1980-09-02 The Dow Chemical Company Composition and method for removing sulfide-containing scale from metal surfaces
EP0012478A3 (en) * 1978-12-06 1980-09-17 The Dow Chemical Company Composition and method for removing sulfide-containing scale from metal surfaces
EP0139567A3 (en) * 1983-09-30 1986-07-23 The Dow Chemical Company Method and composition for inhibiting corrosion
EP0139567A2 (en) * 1983-09-30 1985-05-02 Pumptech N.V. Method and composition for inhibiting corrosion
US4680127A (en) * 1985-12-13 1987-07-14 Betz Laboratories, Inc. Method of scavenging hydrogen sulfide
US5152916A (en) * 1989-08-23 1992-10-06 Hoechst Aktiengesellschaft Aqueous aldehyde solutions for trapping hydrogen sulfide in natural gas and crude oil producing plants
US5225103A (en) * 1989-08-23 1993-07-06 Hoechst Aktiengesellschaft Aqueous aldehyde solutions for trapping hydrogen sulfide in natural gas and crude oil producing plants
US5085842A (en) * 1990-01-25 1992-02-04 Hoechst Aktiengesellschaft Process for scavenging hydrogen sulfide using glyoxal
US5854180A (en) * 1998-03-24 1998-12-29 Clearwater, Inc. Environmentally improved acid corrosion inhibitor
EP0947608A1 (en) * 1998-03-24 1999-10-06 Clearwater, Inc. Environmentally benign acid corrosion inhibitor
US6666975B1 (en) 2002-10-04 2003-12-23 Ge Betz, Inc. Method of reducing hydrogen sulfide odor emissions from an aqueous medium
EP1624089A1 (en) 2004-07-08 2006-02-08 General Electric Company Method of preventing hydrogen sulfide odor generation in an aqueous medium
US20060073112A1 (en) * 2004-10-01 2006-04-06 Whitekettle Wilson K Method of preventing hydrogen sulfide odor generation in an aqueous medium
US20070131625A1 (en) * 2005-12-12 2007-06-14 General Electric Company Methods of inhibiting biogenic sulfide formation in aqueous systems
US20090068059A1 (en) * 2007-09-12 2009-03-12 Whitekettle Wilson K Method of preventing hydrogen sulfide odor generation in an aqueous medium
US20110100630A1 (en) * 2009-11-02 2011-05-05 Baker Hughes Incorporated Method of Mitigating Corrosion Rate of Oilfield Tubular Goods
US20130112106A1 (en) * 2011-11-08 2013-05-09 Mark A. Malwitz Environmentally friendly corrosion inhibitor
US9074289B2 (en) * 2011-11-08 2015-07-07 Nalco Company Environmentally friendly corrosion inhibitor
US20170175275A1 (en) * 2013-09-23 2017-06-22 Agienic, Inc. Compositions For Use In Corrosion Protection
US10400339B2 (en) * 2013-09-23 2019-09-03 Agienic, Inc. Low water solubility compositions for use in corrosion protection
US10072339B2 (en) * 2013-09-23 2018-09-11 Agienic, Inc. Compositions for use in corrosion protection
US10392712B2 (en) 2013-10-24 2019-08-27 Baker Hughes, A Ge Company, Llc Chemical inhibition of pitting corrosion in methanolic solutions containing an organic halide
US9732430B2 (en) 2013-10-24 2017-08-15 Baker Hughes Incorporated Chemical inhibition of pitting corrosion in methanolic solutions containing an organic halide
WO2015142633A1 (en) 2014-03-18 2015-09-24 Baker Hughes Incorporated Dimercaptothiadiazoles to prevent corrosion of mild steel by acid gases in oil and gas products
US9663666B2 (en) 2015-01-22 2017-05-30 Baker Hughes Incorporated Use of hydroxyacid to reduce the localized corrosion potential of low dose hydrate inhibitors
WO2016118400A1 (en) 2015-01-22 2016-07-28 Baker Hughes Incorporated Use of hydroxyacid to reduce the localized corrosion potential of low dose hydrate inhibitors
US11034921B2 (en) 2018-05-16 2021-06-15 Adam Mason PRINCE Method, kit, and composition for corrosion removal
WO2022178251A1 (en) 2021-02-19 2022-08-25 Nissan Chemical America Corporation Use of silica nanoparticles with glyoxal for h2s scavenging

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