USRE30283E - Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions - Google Patents
Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions Download PDFInfo
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- USRE30283E USRE30283E US06/011,745 US1174579A USRE30283E US RE30283 E USRE30283 E US RE30283E US 1174579 A US1174579 A US 1174579A US RE30283 E USRE30283 E US RE30283E
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- 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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
- C23G1/04—Cleaning or pickling metallic material with solutions or molten salts with acid solutions using inhibitors
- C23G1/06—Cleaning or pickling metallic material with solutions or molten salts with acid solutions using inhibitors organic inhibitors
- C23G1/065—Cleaning or pickling metallic material with solutions or molten salts with acid solutions using inhibitors organic inhibitors sulfur-containing compounds
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/34—Organic compounds containing sulfur
Definitions
- Iron oxide encrustations commonly known as rust or iron oxide scale, frequently form on ferrous metal surfaces.
- Such surface deposits are objectionable on ferrous articles which are scheduled to be refinished (e.g. sheet steel) and are particularly troublesome when located on the surfaces of tubing and other conduits (e.g., boiling tubing, heat exchangers, connecting piping, and the like) wherein the deposits can restrict flow and interfere with heat exchange.
- aqueous acidic cleaning solution e.g. aqueous HCl
- An iron salt typically results from this operation, the specific salt depending upon the acidic cleaning medium used.
- FeCl 3 and/or FeCl 2 are formed when HCl is used.
- Such iron salts are generally soluble to at least a limited extent in the cleaning media. Ferric ions thus result.
- Another object of this invention is to inhibit acid induced corrosion of ferrous metal surfaces even in the presence of ferric ions.
- the sulfonium salts represented by I and II below are highly effective in inhibiting the corrosion of metals, particularly ferrous and cuprous metals, in contact with aqueous acid solutions.
- the sulfonium salts correspond to the formula ##STR2## wherein n is 1 or 2; each R 1 independently is hydrogen or a hydrocarbyl, hydrocarbyloxy or hydrocarbylthio radical of from 1 to about 24 carbon atoms; R 2 is a hydrocarbyl or inertly-substituted hydrocarbyl radical of from 1 to about 24 carbon atoms, with the proviso that the total aggregate carbon content of R 1 and R 2 is from 7 to about 25; R 3 is an alkyl radical of from 1 to 4 carbon atoms or an inertly-substituted alkyl radical of from 2 to 4 carbon atoms, allyl, phenyl or an inertly-substituted phenyl radical; or R 2 and R 3 are joined to
- the sulfonium salts represented by I and II are effective at low concentrations (e.g. 2 to 4 millimoles/liter) and are, surprisingly, effective even in the presence of ferric ions.
- ferric ion corrosion problem experienced during the cleaning of ferrous metal surfaces can be substantially reduced if not eliminated by incorporating into the acidic cleaning solution a small but sufficient amount of said sulfonium salts to produce the desired inhibition effect.
- Suitable sulfonium salts for use herein are represented by I and II above, each of which represents a known class of compounds. Such compounds are typically prepared in a known reaction comprising reacting a "benzyl" halide with an appropriate sulfide, as per the equation: ##STR3## In this illustration, of course, X is halogen (e.g. chloro or bromo) and becomes the anion (A.sup. ⁇ ) in the final product (I or II). The corresponding sulfonium salts containing other anions are then typically prepared by conventional ion-exchange techniques. Other methods of preparing I and II are known to those skilled in the art.
- Suitable sulfonium salts are those in I and II wherein:
- R 1 is hydrogen or a hydrocarbyl radical, such as alkyl (e.g. methyl, ethyl, propyl, butyl, hexyl, octyl, decyl, dodecyl, and the like), aryl (e.g. phenyl, naphthyl, and the like), aralkyl (e.g. benzyl, phenethyl, and the like), alkaryl (e.g. tolyl, 3,5-dimethylphenyl, butylphenyl, and the like), cycloalkyl (e.g. cyclohexyl and the like), alkenyl (e.g.
- hydrocarbyloxy such as alkoxy, aryloxy, alkenyloxy, etc. (e.g. butoxy, phenoxy, p-hydroxyphenoxy, hexylphenoxy, chlorophenoxy, allyloxy, and the like); or hydrocarbylthio radicals, such as alkylthio, arylthio, etc. (e.g. methylthio, ethylthio, butylthio, phenylthio, and the like);
- R 2 is a hydrocarbyl radical, such as alkyl (e.g. methyl, ethyl, propyl, butyl, hexyl, octyl, decyl, dodecyl, and the like), aryl (e.g. phenyl, hydroxyphenyl and the like), aralkyl (e.g. benzyl, phenethyl phenylbutyl, and the like), alkaryl (e.g. tolyl, 3,5-dimethylphenyl, butylphenyl, hexylphenyl, and the like), cycloalkyl (e.g. cyclohexyl, and the like), alkenyl (e.g. allyl, butenyl, hexenyl, and the like; or
- R 3 is an alkyl radical of from 1 to 4 carbon atoms (i.e. methyl, ethyl, propyl and butyl) or an inertly-substituted alkyl radical of 1 to 4 carbon atoms, allyl, phenyl or inertly-substituted phenyl.
- inertly-substituted as used in this application is meant that the hydrocarbyl radical bears one or more substituents which are inert to the liquid acidic medium in which the sulfonium corrosion inhibitors are to be used. Such inert substituents include hydroxy, halo, etc.
- R 3 includes hydroxyalkyl radicals of 1 to 4 carbon atoms, chloroalkyl radicals, and the like;
- R 2 and R 3 can be joined to form, in combination with the sulfonium atom, a 5- or 6-membered heterocyclic ring (such as thiophenium, tetrahydrothiophenium, thiopyrylium and tetrahydrothiopyrylium);
- A.sup. ⁇ is a compatible anion.
- the choice of anion, A.sup. ⁇ is not critical and may be varied to convenience. However, the anion is generally chosen to be the same as the acid in solution as a matter of convenience.
- the anion may be selected by the method of preparing the sulfonium salt or by ion exchange means. Examples of suitable anions include chloride, bromide, iodide, nitrate, bisulfate, tosylate, acetate, benzoate, dihydrogen phosphate, and the like.
- R 1 is preferably a meta- or para-substituent (most preferably para) in I.
- n 1 in I and II.
- R 1 is preferably hydrogen, alkyl or alkylphenoxy and is most preferably alkyl of 8 to 18 carbon atoms.
- R 2 is preferably alkyl, ⁇ -hydroxyalkyl of 2 to 4 carbon atoms (i.e. ⁇ -hydroxyethyl, ⁇ -hydroxypropyl and ⁇ -hydroxybutyl), allyl, phenyl or hydroxyphenyl, and is most preferably alkyl, ⁇ -hydroxyethyl or allyl.
- R 3 is preferably alkyl of 1 to 4 carbon atoms, ⁇ -hydroxyalkyl of 2 to 4 carbon atoms, allyl, phenyl or hydroxyphenyl, and is most preferably alkyl of 1 to 4 carbon atoms, ⁇ -hydroxyethyl or allyl.
- the preferred sulfonium salts are, of course, a combination of the above preferences for R 1 -R 3 and n.
- the most preferred sulfonium salts are a combination of the most preferred embodiments for R 1 -R 3 with n being 1.
- the sulfonium salts represented by Formula I are normally preferred over those represented by Formula II.
- Suitable sulfonium salts for use herein include those in Formula I having the following values for R 1 -R 3 and A.sup. ⁇ .
- the sulfonium compounds within Formula II having corresponding R 1 -R 3 and A.sup. ⁇ values are likewise representative compounds of the sulfonium salts within Formula II.
- Other suitable compounds include the following: ##STR5## wherein n is 1 in each case and R 1 and A.sup. ⁇ have the following values:
- the acid solutions suitable for use herein are aqueous solutions of non-oxidizing inorganic acids, such as HF, HCl, H 2 SO 4 , H 3 PO 4 , etc., and mixtures thereof (oxidizing inorganic acids include HNO 3 , HClO 4 , CrO 3 , etc.); or aqueous solutions of organic acids, such as formic acid acetic acid, sulfamic acid, hydroxy acetic, citric acid, etc., and mixtures thereof; or are aqueous solutions of known chelating agents, such as ethylenediaminetetraacetic acid, hereafter EDTA (and the ammonium, amine, or alkali metal salts of EDTA), and other like polyaminepolycarboxylic acids and the like; and mixtures of such aqueous acid solutions.
- non-oxidizing inorganic acids include HNO 3 , HClO 4 , CrO 3 , etc.
- organic acids such as formic acid acetic acid,
- the most common cleaning solutions are aqueous solutions of HCl and aqueous solutions of EDTA and amine or alkali metal salts of EDTA.
- the acid solutions may be buffered to maintain a desired pH level with conventional buffering agents, such as citric acid, acetic acid, and salts thereof.
- the pH values of acid cleaning solutions typically range from 1 to 5 for aqueous solutions of organic acids, and from pH 2-5 for aqueous solutions of chelating agents, such as the EDTA type cleaning solutions.
- the normality of cleaning solutions using inorganic acids are typically greater than 1.
- concentration of sulfonium salt used in the acid solutions may vary depending upon the particular salt, the particular metal and the degree of corrosion inhibition desired. Typically, concentrations of from about 1 ⁇ 10 -6 to about 0.1 moles of sulfonium salt per liter of solution are sufficient and concentrations of from about 1 ⁇ 10 -4 to 0.01 moles/liter are generally preferred.
- Coupons of carbon steel having approximately 40 square centimeters of surface area were (a) scrubbed thoroughly with a soap-filled pad of steel wool in warm water, (b) rinsed with water, (c) washed with acetone, (d) pickled for 5 minutes in 10% aqueous HCl, (e) dried in air, and (f) weighed.
- the coupons thus prepared were then suspended from glass hooks in a stirred acid cleaning solution at 25° C. or 50° C. for normally 16 hours; the coupons being completely immersed in the solution.
- the coupons were then removed from the acid solutions, washed with soap and warm water, rinsed, dried and weighed.
- the weight loss resulting from such treatment is a measure of corrosion.
- the weight loss rate (WLR) having the units lbs./ft 2 /day is determined as follows: ##EQU1## wherein
- (a) 49.15 is a conversion factor for converting gm./cm. 2 /hr. to lbs./ft 2 /day;
- the quantity of acid cleaning solution in each case was approximately 1400 milliliters.
- Solution “A” was a 3.8 percent by weight, total weight basis, aqueous solution of an ammonium salt of ethylenediaminetetracetic acid buffered at a pH of 5 with citric acid and contained 0.10 percent by weight, total weight basis, of Fe +3 (added as FeNH 4 (SO 4 ) 2 . 12 H 2 O).
- Solution “B” was a 10 percent by weight, total weight basis, aqueous solution of HCl, and 0.10 percent by weight of Fe +3 (added as FeCl 3 ).
- Solution “C” was a 10 percent by weight, total weight basis, aqueous solution of H 2 SO 4 and 0.1 percent by weight of Fe +3 (added as FeNH 4 (SO 4 ) 2 . 12H 2 O).
- the R 1 radical was actually a mixture of C 8 -C 18 alkyl radicals with C 12 H 25 being the predominant species.
- test solution "A” containing p-n-dodecylbenzyldimethylsulfonium chloride as the inhibitor was evaluated in a "flow test" wherein the solution was pumped through steel pipes for 6 to 7 hours and the degree of corrosion determined as above.
- the steel pipes used in this test were sections cut from the same length of pipe and measured approximately 1 foot in length and 0.75 inch in inside diameter.
- the pipes were cleaned free of rust by use of a commercial cleaning solution quite similar to solution "A” except that no Fe +3 was added, and were scrubbed with soap and warm water, rinsed with water, rinsed with acetone, dried and weighed. After the flow test, the pipes were again scrubbed, rinsed with water, rinsed with acetone, dried and weighed.
- the subject sulfonium salts were evaluated as corrosion inhibitors in aqueous acid solutions which did not initially contain any significant amount of ferric ion.
- Experiments 24 and 25 were conducted in 10 percent by weight, total weight basis, aqueous HCl solutions and experiment 26 was conducted in a 10 percent by weight aqueous H 2 SO 4 solution.
- the inhibitor was p-dodecylbenzyldimethylsulfonium chloride and the metal coupons and the testing procedure used were substantially the same as described in experiments 1-10. The results are tabulated in Table VII below.
- the concentration (Conc.) of sulfonium salt is expressed in millimoles per liter.
- coupons cleaned with the test solutions inhibited with p-dodecylbenzyldimethylsulfonium chloride were observed to have a protective film of (predominantly) (p,p'-bisdodecyl)bibenzyl and p-dodecyltoluene on their surface; such coupons were suspended over water in a closed vessel for 11 days and showed only small localized rust spots while coupons cleaned with the uninhibited solutions and concurrently aged over water were uniformly covered with red rust.
- the compounds used in experiments 46 and 47 are illustrative of sulfonium salts corresponding to the general formula ##STR12## wherein: R 2 and R 3 have the aforesaid meaning; R 4 is alkyl of 4 to about 20 carbon atoms; R 5 is methyl or ethyl; R 6 is hydrogen, methyl or ethyl; q is an integer of from 0 to 8; r is an integer of from 0 to 10; with the proviso that the sum of q plus r is equal to or less than 10.
- Such compounds are conveniently prepared by reacting a xylyl dihalide (e.g.
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Abstract
Certain sulfonium salts are herein described which are useful corrosion inhibitors in aqueous acidic cleaning solutions, even in the presence of ferric ions. The sulfonium salts correspond to the following formulas: ##STR1##
Description
This application is a continuation of our U.S. patent application Ser. No. 350,295 filed Apr. 11, 1973 (now abandoned) which is a continuation-in-part of our U.S. patent application Ser. No. 118,175 filed Feb. 23, 1971 (and is now USP 3,764,543).
Iron oxide encrustations, commonly known as rust or iron oxide scale, frequently form on ferrous metal surfaces. Such surface deposits are objectionable on ferrous articles which are scheduled to be refinished (e.g. sheet steel) and are particularly troublesome when located on the surfaces of tubing and other conduits (e.g., boiling tubing, heat exchangers, connecting piping, and the like) wherein the deposits can restrict flow and interfere with heat exchange.
Various methods of removing such surface deposits have been devised, a common one being to contact the ferrous surface with an aqueous acidic cleaning solution (e.g. aqueous HCl) and thereby dissolve and remove the iron oxide encrustations from the surface. An iron salt typically results from this operation, the specific salt depending upon the acidic cleaning medium used. E.g., FeCl3 and/or FeCl2 are formed when HCl is used.
Such iron salts are generally soluble to at least a limited extent in the cleaning media. Ferric ions thus result.
Corrosion of ferrous metal surfaces in contact with aqueous acids is known. It is also known that the presence of ferric ion causes severe corrosion problems of ferrous metal surfaces during the above mentioned acid cleaning process. Namely, the cleaning solution attacks (corrodes) the freshly cleaned metal surface with the attendant loss of metal. In the presence of oxygen, ferric ions are continually regenerated accentuating the problem.
Many compounds have been included as corrosion inhibitors in such cleaning solutions but their effectiveness in the presence of ferric ion is generally nonexistent or quite low.
Similarly, the corrosion of other common construction metals (and metal alloys) in contact with aqueous acid solution is a definite problem. E.g., in the abovementioned process of clearing ferrous metal surfaces with acid solutions, other metals may be present as an integral part of the system being cleaned (e.g. copper, copper alloys, zinc, zinc alloys, stainless steels, etc.), which may be similarly corroded.
It is therefore an object of this invention to inhibit the acid induced corrosion of metal surfaces, particularly ferrous and cuprous metal surfaces, in contact with aqueous acid solutions.
Another object of this invention is to inhibit acid induced corrosion of ferrous metal surfaces even in the presence of ferric ions.
It has now been discovered that the sulfonium salts represented by I and II below are highly effective in inhibiting the corrosion of metals, particularly ferrous and cuprous metals, in contact with aqueous acid solutions. The sulfonium salts correspond to the formula ##STR2## wherein n is 1 or 2; each R1 independently is hydrogen or a hydrocarbyl, hydrocarbyloxy or hydrocarbylthio radical of from 1 to about 24 carbon atoms; R2 is a hydrocarbyl or inertly-substituted hydrocarbyl radical of from 1 to about 24 carbon atoms, with the proviso that the total aggregate carbon content of R1 and R2 is from 7 to about 25; R3 is an alkyl radical of from 1 to 4 carbon atoms or an inertly-substituted alkyl radical of from 2 to 4 carbon atoms, allyl, phenyl or an inertly-substituted phenyl radical; or R2 and R3 are joined to form a 5- or 6-membered heterocyclic ring, with the proviso that the total aggregate carbon content of R1, R2 and R3 is from 10 to about 25 when R2 is joined with R3 to form a 5- or 6-membered ring; and A.sup.⊖ is an anion.
The sulfonium salts represented by I and II are effective at low concentrations (e.g. 2 to 4 millimoles/liter) and are, surprisingly, effective even in the presence of ferric ions. Thus, the above-described ferric ion corrosion problem experienced during the cleaning of ferrous metal surfaces can be substantially reduced if not eliminated by incorporating into the acidic cleaning solution a small but sufficient amount of said sulfonium salts to produce the desired inhibition effect.
Suitable sulfonium salts for use herein are represented by I and II above, each of which represents a known class of compounds. Such compounds are typically prepared in a known reaction comprising reacting a "benzyl" halide with an appropriate sulfide, as per the equation: ##STR3## In this illustration, of course, X is halogen (e.g. chloro or bromo) and becomes the anion (A.sup.⊖) in the final product (I or II). The corresponding sulfonium salts containing other anions are then typically prepared by conventional ion-exchange techniques. Other methods of preparing I and II are known to those skilled in the art.
Examples of suitable sulfonium salts are those in I and II wherein:
R1 is hydrogen or a hydrocarbyl radical, such as alkyl (e.g. methyl, ethyl, propyl, butyl, hexyl, octyl, decyl, dodecyl, and the like), aryl (e.g. phenyl, naphthyl, and the like), aralkyl (e.g. benzyl, phenethyl, and the like), alkaryl (e.g. tolyl, 3,5-dimethylphenyl, butylphenyl, and the like), cycloalkyl (e.g. cyclohexyl and the like), alkenyl (e.g. vinyl, allyl, butenyl, hexenyl, and the like); or hydrocarbyloxy, such as alkoxy, aryloxy, alkenyloxy, etc. (e.g. butoxy, phenoxy, p-hydroxyphenoxy, hexylphenoxy, chlorophenoxy, allyloxy, and the like); or hydrocarbylthio radicals, such as alkylthio, arylthio, etc. (e.g. methylthio, ethylthio, butylthio, phenylthio, and the like);
R2 is a hydrocarbyl radical, such as alkyl (e.g. methyl, ethyl, propyl, butyl, hexyl, octyl, decyl, dodecyl, and the like), aryl (e.g. phenyl, hydroxyphenyl and the like), aralkyl (e.g. benzyl, phenethyl phenylbutyl, and the like), alkaryl (e.g. tolyl, 3,5-dimethylphenyl, butylphenyl, hexylphenyl, and the like), cycloalkyl (e.g. cyclohexyl, and the like), alkenyl (e.g. allyl, butenyl, hexenyl, and the like; or
R3 is an alkyl radical of from 1 to 4 carbon atoms (i.e. methyl, ethyl, propyl and butyl) or an inertly-substituted alkyl radical of 1 to 4 carbon atoms, allyl, phenyl or inertly-substituted phenyl. By "inertly-substituted" as used in this application is meant that the hydrocarbyl radical bears one or more substituents which are inert to the liquid acidic medium in which the sulfonium corrosion inhibitors are to be used. Such inert substituents include hydroxy, halo, etc. Thus, R3 includes hydroxyalkyl radicals of 1 to 4 carbon atoms, chloroalkyl radicals, and the like;
R2 and R3 can be joined to form, in combination with the sulfonium atom, a 5- or 6-membered heterocyclic ring (such as thiophenium, tetrahydrothiophenium, thiopyrylium and tetrahydrothiopyrylium);
with the proviso that the total aggregate carbon content of R1 and R2 is from 7 to about 25; and, with the additional proviso that the total aggregate carbon content of R1, R2 and R3 is from 10 to about 25 when R2 and R3 are joined to form the 5- or 6-membered heterocyclic rings;
A.sup.⊖ is a compatible anion. The choice of anion, A.sup.⊖ is not critical and may be varied to convenience. However, the anion is generally chosen to be the same as the acid in solution as a matter of convenience. The anion may be selected by the method of preparing the sulfonium salt or by ion exchange means. Examples of suitable anions include chloride, bromide, iodide, nitrate, bisulfate, tosylate, acetate, benzoate, dihydrogen phosphate, and the like. The ring position of the R1 substituent(s) in I and II is not critical but is preferably at least two ring carbons removed from the --CH2 --S.sup.⊕ R2 R3 A.sup.⊖ group. E.g. R1 is preferably a meta- or para-substituent (most preferably para) in I.
Preferably, n is 1 in I and II.
R1 is preferably hydrogen, alkyl or alkylphenoxy and is most preferably alkyl of 8 to 18 carbon atoms.
R2 is preferably alkyl, β-hydroxyalkyl of 2 to 4 carbon atoms (i.e. β-hydroxyethyl, β-hydroxypropyl and β-hydroxybutyl), allyl, phenyl or hydroxyphenyl, and is most preferably alkyl, β-hydroxyethyl or allyl.
R3 is preferably alkyl of 1 to 4 carbon atoms, β-hydroxyalkyl of 2 to 4 carbon atoms, allyl, phenyl or hydroxyphenyl, and is most preferably alkyl of 1 to 4 carbon atoms, β-hydroxyethyl or allyl.
The preferred sulfonium salts are, of course, a combination of the above preferences for R1 -R3 and n. Likewise, the most preferred sulfonium salts are a combination of the most preferred embodiments for R1 -R3 with n being 1. Additionally, the sulfonium salts represented by Formula I are normally preferred over those represented by Formula II.
Representative examples of suitable sulfonium salts for use herein include those in Formula I having the following values for R1 -R3 and A.sup.⊖.
Table I
__________________________________________________________________________
##STR4## I
R.sub.1 R.sub.2 R.sub.3 A.sup.⊖
__________________________________________________________________________
CH.sub.3 C.sub.18 H.sub.37
CH.sub.3 Cl
C.sub.3 H.sub.7
C.sub.10 H.sub.21
C.sub.2 H.sub.5
HSO.sub.4
C.sub.6 H.sub.13
CH.sub.3 C.sub.6 H.sub.5
Cl
C.sub.3 H.sub.17
CH.sub.2CHCH.sub.2
CH.sub.2CHCH.sub.2
Br
C.sub.12 H.sub.25
CH.sub.3 CH.sub.2 CH.sub.2 OH
Cl
C.sub.18 H.sub.37
CH.sub.3 CH.sub.3 I
C.sub.20 H.sub.41
CH.sub.3 CH.sub.2CHCH.sub.2
Cl
C.sub.8 H.sub.17 O
CH.sub.2 CH.sub.2 OH
CH.sub.2 CH.sub.2 OH
NO.sub.3
C.sub.4 H.sub.9 S
C.sub.12 H.sub.25
C.sub.3 H.sub.7
tosylate
C.sub.6 H.sub.5
CH.sub.3 CH.sub.3 H.sub.2 PO.sub.4
C.sub.6 H.sub.5 O
C.sub.6 H.sub.13
CH.sub.3 acetate
C.sub.4 H.sub.9 C.sub.6 H.sub.4 O
CH.sub.2 CH.sub. 2 OH
CH.sub.2 CH.sub.2 OH
Cl
C.sub.8 H.sub.17 C.sub.6 H.sub.4 O
CH.sub.3 CHCHCH.sub.2
C.sub.4 H.sub.9
Br
C.sub.6 H.sub.5 CH.sub.2 CH.sub.2
C.sub.3 H.sub.7
C.sub.3 H.sub.7
I
cyclohexyl C.sub.4 H.sub.9
CH.sub.3 NO.sub.1
C.sub.6 H.sub.5 S
CH.sub.3 C.sub.6 H.sub.5 OH
Cl
H C.sub.6 H.sub.5 CH.sub.2 CH.sub.2
CH.sub.3 HSO.sub.4
CH.sub.2CH C.sub.18 H.sub.37
CH.sub.3 Cl
CH.sub.2CHCH.sub.2
C.sub.12 H.sub.25
C.sub.2 H.sub.4
Cl
CH.sub.2CHCH.sub.2O
C.sub.6 H.sub.13
CH.sub.3 I
3-ethyl, 5-ethyl
C.sub.8 H.sub.17
CH.sub.2 CH.sub.2 OH
Cl
2-methyl, 4-methyl
C.sub.18 H.sub.37
CH.sub.3 Br
__________________________________________________________________________
The sulfonium compounds within Formula II having corresponding R1 -R3 and A.sup.⊖ values are likewise representative compounds of the sulfonium salts within Formula II. Other suitable compounds include the following: ##STR5## wherein n is 1 in each case and R1 and A.sup.⊖ have the following values:
Table II
______________________________________
R.sub.1 A.sup.⊖
______________________________________
C.sub.6 H.sub.13
Cl
C.sub.8 H.sub.17
Br
C.sub.10 H.sub.21
I
C.sub.12 H.sub.25
HSO.sub.4
C.sub.18 H.sub.37
Cl
______________________________________
The above examples are merely illustrative and other like compounds within I and II will be so readily apparent to those skilled in the art.
The acid solutions suitable for use herein are aqueous solutions of non-oxidizing inorganic acids, such as HF, HCl, H2 SO4, H3 PO4, etc., and mixtures thereof (oxidizing inorganic acids include HNO3, HClO4, CrO3, etc.); or aqueous solutions of organic acids, such as formic acid acetic acid, sulfamic acid, hydroxy acetic, citric acid, etc., and mixtures thereof; or are aqueous solutions of known chelating agents, such as ethylenediaminetetraacetic acid, hereafter EDTA (and the ammonium, amine, or alkali metal salts of EDTA), and other like polyaminepolycarboxylic acids and the like; and mixtures of such aqueous acid solutions. The most common cleaning solutions are aqueous solutions of HCl and aqueous solutions of EDTA and amine or alkali metal salts of EDTA. The acid solutions may be buffered to maintain a desired pH level with conventional buffering agents, such as citric acid, acetic acid, and salts thereof. The pH values of acid cleaning solutions typically range from 1 to 5 for aqueous solutions of organic acids, and from pH 2-5 for aqueous solutions of chelating agents, such as the EDTA type cleaning solutions. The normality of cleaning solutions using inorganic acids are typically greater than 1.
The concentration of sulfonium salt used in the acid solutions may vary depending upon the particular salt, the particular metal and the degree of corrosion inhibition desired. Typically, concentrations of from about 1×10-6 to about 0.1 moles of sulfonium salt per liter of solution are sufficient and concentrations of from about 1×10-4 to 0.01 moles/liter are generally preferred.
The following examples further illustrate the invention.
Coupons of carbon steel (having 98.7% Fe; 0.3% Mn; and 0.05% C.) having approximately 40 square centimeters of surface area were (a) scrubbed thoroughly with a soap-filled pad of steel wool in warm water, (b) rinsed with water, (c) washed with acetone, (d) pickled for 5 minutes in 10% aqueous HCl, (e) dried in air, and (f) weighed. The coupons thus prepared were then suspended from glass hooks in a stirred acid cleaning solution at 25° C. or 50° C. for normally 16 hours; the coupons being completely immersed in the solution. The coupons were then removed from the acid solutions, washed with soap and warm water, rinsed, dried and weighed. The weight loss resulting from such treatment is a measure of corrosion. The weight loss rate (WLR), having the units lbs./ft2 /day is determined as follows: ##EQU1## wherein
(a) 49.15 is a conversion factor for converting gm./cm.2 /hr. to lbs./ft2 /day; (b) SF=strip factor=average ratio of surface area (cm.2) to weight (gm.); and (c) the time is measured in hours. The quantity of acid cleaning solution in each case was approximately 1400 milliliters.
The effectiveness of the sulfonium salts was determined by comparing the WLR of a cleaning solution containing the sulfonium salts (WLR (test)) against the WLR of an identical cleaning solution without the sulfonium salts (WLR (blank)). The comparative data is reported as the "Percent Protection" which is calculated as follows: ##EQU2##
The sulfonium salts were evaluated in three representative acid cleaning solutions. Solution "A" was a 3.8 percent by weight, total weight basis, aqueous solution of an ammonium salt of ethylenediaminetetracetic acid buffered at a pH of 5 with citric acid and contained 0.10 percent by weight, total weight basis, of Fe+3 (added as FeNH4 (SO4)2. 12 H2 O). Solution "B" was a 10 percent by weight, total weight basis, aqueous solution of HCl, and 0.10 percent by weight of Fe+3 (added as FeCl3). Solution "C" was a 10 percent by weight, total weight basis, aqueous solution of H2 SO4 and 0.1 percent by weight of Fe+3 (added as FeNH4 (SO4)2. 12H2 O).
The results of several experiments conducted in accordance with the above general procedure and using solution "A" containing various inhibitors are tabulated in Table III. The sulfonium salts used in this series of experiments correspond to Formula I wherein n is 1, A.sup.⊖ is chloride and R1 -R3 are as designated in the table. The concentration of the sulfonium salts in the test solutions is listed in Table III (and the remaining tables herein) under the heading "Conc." and is expressed in millimoles (m-moles) per liter. The steel metal coupons having the above assay were used in every one of the following examples unless otherwise specified.
Table III
__________________________________________________________________________
Temp.
WLR %
Ex.
R.sub.1
R.sub.2
R.sub.3
Conc.
(°C.)
(Test)
Protection
__________________________________________________________________________
1 CH.sub.3
C.sub.12 H.sub.25
CH.sub.3
0.40
25 0.0571
26
2 i-C.sub.3 H.sub.7
C.sub.12 H.sub.25
CH.sub.3
0.40
25 0.0267
64
3 p-n-C.sub.8 H.sub.17
CH.sub.3
CH.sub.3
0.69
50 0.0054
89
4 p-n-C.sub.12 H.sub.25
CH.sub.3
0.20 25 0.0020
95
5 p-n-C.sub.12 H.sub.25
CH.sub.3
CH.sub.3
0.30
50 0.0090
82
6 p-n-C.sub.12 H.sub.25
CH.sub.3
n-C.sub.4 H.sub.9
0.40
25 0.0039
90
7 p-n-C.sub.12 H.sub.25
CH.sub.2 CH.sub.2 OH
CH.sub.2 CH.sub.2 OH
0.20
25 0.003
93
8 p-n-C.sub.12 H.sub.25
n-C.sub.4 H.sub.4
n-C.sub.4 H.sub.9
0.40
25 0.025
34
9 p-n-C.sub.12 H.sub.25
n-C.sub.12 H.sub.25
CH.sub.3
0.04
25 0.072
6
10 p-C.sub.17 H.sub.35
CH.sub.3
CH.sub.3
0.30
50 0.020
61
__________________________________________________________________________
In experiments 4-9, the R1 radical was actually a mixture of C8 -C18 alkyl radicals with C12 H25 being the predominant species.
In like manner, benzyldodecylmethylsulfonium bromide gave 8 percent protection under similar circumstances (solution "A", Conc.=0.4, 25° C., WLR of 0.035).
In like manner, certain sulfonium salts represented by I were shown to be effective in inhibiting corrosion by solution "B". In each instance, A.sup.⊖ is chloride and n is 1 in Formula I. Data are in Table IV below:
Table TV
__________________________________________________________________________
Temp.
WLR %
Ex.
R.sub.1
R.sub.2
R.sub.3
Conc.
(°C.)
(Test)
Protection
__________________________________________________________________________
12 p-n-C.sub.12 H.sub.25
CH.sub.3
CH.sub.3
0.20
25 0.020
52
13 p-n-C.sub.12 H.sub.25
CH.sub.CH.sub.3
0.39 0.39
50 0.021
69
14 p-n-C.sub.2 H.sub.17
CH.sub.3
CH.sub.3
0.40
25 0.029
52
15 p-n-C.sub.12 H.sub.25
CH.sub.2 CH.sub.2 OH
CH.sub.2 CH.sub.2 OH
0.40
25 0.018
56
__________________________________________________________________________
In like manner, certain sulfonium salts represented by I were shown to be effective in inhibiting corrosion by solution "C". In each instance, A.sup.⊖ is chloride and n is 1 in Formula I. Data are in Table V below:
Table V
______________________________________
Temp. WLR % Pro-
Ex. R.sub.1 R.sub.2
R.sub.3
Conc. (°C.)
(Test)
tection
______________________________________
16 p-n-C.sub.12 H.sub.25
CH.sub.3
CH.sub.3
0.40 25 0.003 94
17 p-n-C.sub.3 H.sub.17
CH.sub.3
CH.sub.3
0.40 25 0.009 93
______________________________________
In other experiments, test solution "A" containing p-n-dodecylbenzyldimethylsulfonium chloride as the inhibitor was evaluated in a "flow test" wherein the solution was pumped through steel pipes for 6 to 7 hours and the degree of corrosion determined as above. The steel pipes used in this test were sections cut from the same length of pipe and measured approximately 1 foot in length and 0.75 inch in inside diameter. The pipes were cleaned free of rust by use of a commercial cleaning solution quite similar to solution "A" except that no Fe+3 was added, and were scrubbed with soap and warm water, rinsed with water, rinsed with acetone, dried and weighed. After the flow test, the pipes were again scrubbed, rinsed with water, rinsed with acetone, dried and weighed. The "WLR" and "Percent Protection" were calculated as above. The results are summarized in Table VI below. The flow rate is measured in gallons/minute and the concentration of sulfonium salt (Conc.) is expressed as millimoles per liter.
Table VI
______________________________________
Flow Temp. Inhibitor
WLR Percent
Ex. Rate (°C.)
Conc. (Test) Protection
______________________________________
18 0.2 25 0.39 0.011 89
19 0.2 50 0.39 0.016 81
20 0.2 65 0.56 0.014 86
21 5.0 25 0.39 0.0064 97
22 5.0 65 0.56 0.028 95
23 10.0 25 0.39 0.0064 99
______________________________________
In still other experiments, the subject sulfonium salts were evaluated as corrosion inhibitors in aqueous acid solutions which did not initially contain any significant amount of ferric ion. Experiments 24 and 25 were conducted in 10 percent by weight, total weight basis, aqueous HCl solutions and experiment 26 was conducted in a 10 percent by weight aqueous H2 SO4 solution. In each of experiments 24-26, the inhibitor was p-dodecylbenzyldimethylsulfonium chloride and the metal coupons and the testing procedure used were substantially the same as described in experiments 1-10. The results are tabulated in Table VII below. The concentration (Conc.) of sulfonium salt is expressed in millimoles per liter.
Table VII
______________________________________
Inhibitor WLR Percent
Ex. Conc. Temp. °C.
(Test) Protection
______________________________________
24 0.28 25 0.0027 91
25 0.36 50 0.0047 98
26 0.30 25 0.0031 75
______________________________________
Using substantially the same procedure and test conditions as in experiment 2, the corrosion of a copper alloy (78% Cu, 21% Zn, and 1% Sn) in contact with solution "A" at 25° C. was found to be inhibited by p-dodecylbenzyldimethylsulfonium chloride (Conc.=0.4 mmoles/liter). WLR (Test)=0.0003. Percent Protection=96%.
Using substantially the same procedure and test conditions as in experiment 2, the corrosion of a ferrous metal coupon (having the aforesaid analysis) in contact with an aqueous 5 percent phosphoric acid solution at 25° C. was found to be inhibited by p-dodecylbenzyldimethylsulfonium chloride (Conc.=0.4 mmoles/liter). WLR (Test)=0.003. Percent Protection=63%.
Using substantially the same procedures and test conditions as detailed in experiments 2, 10 and 15, the corrosion of ferrous metal coupons (having the aforesaid analysis) in contact with solution A, B or C was inhibited by using p-n-dodecylbenzylthiophenium chloride ##STR6## at a concentration of 0.40 mmoles per liter. The temperature in each instance was 25° C. Data are reported in Table VIII.
Table VIII ______________________________________ Ex. Acidic Solution Percent Protection ______________________________________ 29 A 94 30 B 49 31 C 95 ______________________________________
Two other sulfonium salts were evaluated using substantially the same procedure and test conditions detailed in experiment 12 (except that the acid solution was 5% HCl containing 0.3% Fe+3 as ferric chloride instead of 0.1% of Fe+3). p-n-Dodecylbenzyldiallylsulfonium chloride gave 42 percent protection and ##STR7## gave 71 percent protection. The temperature was 25° C. and the concentration of sulfonium salt in the acid medium was about 0.2 mmoles per liter in each instance.
Using substantially the same procedure and test conditions as detailed in experiment 2, the sulfonium salt ##STR8## was evaluated as an inhibitor at a concentration of 0.4 mmoles/liter in solutions "B" and "C" at a temperature of 25° C. The sulfonium salt gave 81 percent and 92 percent protection in solutions "B" and "C", respectively.
Using substantially the same procedure and test conditions detailed in experiment 2, p-dodecylbenzyldodecylmethylsulfonium chloride was evaluated as an inhibitor at a concentration of 0.4 mmoles/liter in solutions "B" and "C" at 25° C. It gave 29 percent and 57 percent protection in solutions "B" and "C", respectively.
In the above examples, a thin, adherent, hydrophobic protective film was generally observed on the ferrous articles cleaned with the inhibited cleaning solutions. The film was predominantly a mixture of compounds of the formula ##STR9## wherein R1 had the designated meaning in the examples. E.g., coupons cleaned with the test solutions inhibited with p-dodecylbenzyldimethylsulfonium chloride were observed to have a protective film of (predominantly) (p,p'-bisdodecyl)bibenzyl and p-dodecyltoluene on their surface; such coupons were suspended over water in a closed vessel for 11 days and showed only small localized rust spots while coupons cleaned with the uninhibited solutions and concurrently aged over water were uniformly covered with red rust.
Using substantially the same procedure and test conditions detailed in experiment 2, the sulfonium salt ##STR10## was evaluated as an inhibitor at a concentration of 0.4 mmoles/liter in solutions "A" and "B". The sulfonium salt gave 73 percent (WLR Test=0.021) and 43 percent (WLR Test=0.025) protection in solutions "A" and "B", respectively. Temperature, 25° C.
Using substantially the same procedure and test conditions detailed in experiment 2, phenoxybenzyldimethylsulfonium chloride was evaluated as an inhibitor at a concentration of 0.4 mmoles in 10 percent aqueous HCl at 25° C. It gave 87 percent protection (WLR Test=0.010). Using the same salt in solutions "A" and "B", the percent protection was 70 percent and 60 percent, respectively.
Using substantially the same procedure and test conditions detailed in experiment 2, dodecylphenoxybenzyldimethylsulfonium chloride was evaluated as an inhibitor at a concentration of 0.4 mmoles/liter in solutions "A" and "B" at 25° C. It gave 87 percent and 43 percent protection in solutions "A" and "B", respectively.
Using substantially the same procedure and test conditions detailed in experiment 2, the effectiveness of sulfonium salts corresponding to the formula ##STR11## wherein q=4 or 7, was evaluated. The data are reported in Table IX.
Table IX
______________________________________
Temp. WLR
Ex. g Conc. (°C.)
(Test) Percent Protection
______________________________________
46 4 0.40 25 0.013 83
47 7 0.40 25 0.026 65
______________________________________
The test solution in these experiments was solution "A".
The compounds used in experiments 46 and 47 are illustrative of sulfonium salts corresponding to the general formula ##STR12## wherein: R2 and R3 have the aforesaid meaning; R4 is alkyl of 4 to about 20 carbon atoms; R5 is methyl or ethyl; R6 is hydrogen, methyl or ethyl; q is an integer of from 0 to 8; r is an integer of from 0 to 10; with the proviso that the sum of q plus r is equal to or less than 10. Such compounds are conveniently prepared by reacting a xylyl dihalide (e.g. ClCH2 --C6 H4 --CH2 Cl) with the sodium alcoholate of an alkoxylated alkylphenol under conventional conditions for a Williamson ether synthesis. The product thus formed is then reacted with R2 --S--R3 to form III, the desired sulfonium compounds.
The above data show that sulfonium salts corresponding to Formulas I-III are effective in inhibiting the corrosion of ferrous and cuprous metals in contact with acidic cleaning solutions and ferric ions. Such experiments are not all inclusive but are merely meant to be illustrative. Other sulfoniums within Formulas I-III can be similarly used.
Claims (20)
1. An aqueous acidic cleaning solution of at least one organic acid having dissolved or dispersed therein a sulfonium salt corresponding to the formula ##STR13## wherein n is 1 or 2; each R1 independently is hydrogen or a hydrocarbyl, a hydrocarbyl whose chain length is interrupted by an atom of oxygen or sulfur, a hydrocarbyloxyor a hydrocarbylthio radical of from 1 to about 24 carbon atoms; R2 is a hydrocarbyl or inertly-substituted hydrocarbyl radical of from 1 to about 24 carbon atoms, with the proviso that the total aggregate carbon content of R1 and R2 is from 7 to about 25; R3 is an alkyl radical of from 1 to 4 carbon atoms or an inertly-substituted alkyl radical of from 2 to 4 carbon atoms, allyl, phenyl or an inertly-substituted phenyl radical; or R2 and R3 are joined to form a 5- or 6-membered heterocyclic ring, with the proviso that the total aggregate carbon content of R1, R2 and R3 is from 10 to about 25; R4 is alkyl of 4 to about 20 carbon atoms; R5 is methyl or ethyl; R6 is hydrogen, methyl or ethyl; q is an integer of from 0 to 8; r is an integer of from 0 to 10, with the proviso that the sum of q plus r is equal to or less than 10; and A.sup.⊖ is an anion; said sulfonium salt being present in an amount at least sufficient to inhibit the acid-induced corrosion of ferrous metals in contact with said solution and ferric ions.
2. The composition defined by claim 1 wherein said sulfonium salt corresponds to Formula I.
3. The composition defined by claim 1 wherein said sulfonium salt corresponds to Formula II.
4. The composition defined by claim 1 wherein said sulfonium salt corresponds to Formula III.
5. The composition defined by claim 1 wherein said sulfonium salt corresponds to Formula I or II and wherein n is 1; R1 is hydrogen, alkyl or alkylphenoxy; R2 is alkyl, β-hydroxyethyl or allyl; R3 is alkyl, β-hydroxyethyl or allyl.
6. In the process of treating ferrous metal surfaces to remove iron oxide encrustations by treating said metal surface with an aqueous acid cleaning solution, the improvement consisting of using the composition defined by claim 1 as said cleaning solution.
7. The composition defined by claim 1 wherein n is 1 and said sulfonium salt corresponds to Formula I and II.
8. The composition defined by claim 7 wherein R1 is hydrogen, alkyl or alkylphenoxy.
9. The composition defined by claim 8 wherein R1 is alkyl of from 8 to 18 carbon atoms.
10. The composition defined by claim 1 wherein R2 is alkyl, β-hydroxyalkyl of 2 to 4 carbon atoms, allyl, phenyl or hydroxyphenyl.
11. The composition defined by claim 10 wherein R2 is alkyl, β-hydroxyethyl or allyl.
12. The composition defined by claim 10 in which R2 and R3 are each alkyl.
13. The composition defined by claim 1 wherein R3 is alkyl, β-hydroxyalkyl of 2 to 4 carbon atoms, allyl, phenyl or hydroxyphenyl.
14. The composition defined by claim 13 wherein R3 is alkyl, β-hydroxyethyl or allyl.
15. The composition defined by claim 14 wherein said sulfonium salt corresponds to Formula I; R1 is alkyl of 8 to 18 carbon atoms; and R2 and R3 are alkyl of 1 to 4 carbon atoms, β-hydroxyethyl or allyl.
16. The composition defined by claim 1 wherein said acid is an aqueous solution of an organic carboxylic or polycarboxylic acid or a mixture thereof.
17. The composition defined by claim 16 wherein said acid is an aqueous solution of a polyaminepolycarboxylic acid or an ammonium-, amine-, or alkali metal salt thereof, or mixtures thereof.
18. The composition defined by claim 17 wherein said acid is an aqueous solution of ethylenediaminetetraacetic acid (EDTA) or the ammonium-, amine-, or alkali metal salt thereof.
19. A process of inhibiting the acid-induced and ferric ion-induced corrosion of metal surfaces in contact with an aqueous acid solution of at least one organic acid, the process comprising incorporating in said acid solution a small but corrosion-inhibiting amount of at least one sulfonium salt corresponding to the formula ##STR14## wherein n is 1 or 2; each R1 independently is hydrogen or a hydrocarbyl, a hydrocarbyl whose chain length is interrupted by an atom of oxygen or sulfur, a hydrocarbyloxy or a hydrocarbylthio radical of from 1 to about 24 carbon atoms; R2 is a hydrocarbyl or inertly-substituted hydrocarbyl radical of from 1 to about 24 carbon atoms, with the proviso that the total aggregate carbon content of R1 and R2 is from 7 to about 25; R3 is an alkyl radical of from 1 to 4 carbon atoms or an inertly-substituted alkyl radical of from 2 to 4 carbon atoms, allyl, phenyl or an inertly-substituted phenyl radical; or R2 and R3 are joined to form a 5- or 6-membered heterocyclic ring, with the proviso that the total aggregate carbon content of R1, R2 and R3 is from 10 to about 25; R4 is alkyl of 4 to about 20 carbon atoms; R5 is methyl or ethyl; R6 is hydrogen, methyl or ethyl; q is an integer of from 1 to 8; r is an integer of from 0 to 12, with the proviso that the sum of q plus r is equal to or less than 12; and A.sup.⊖ is an anion; said sulfonium salt being present in an amount at least sufficient to inhibit the acid-induced corrosion of ferrous metals in contact with said solution and ferric ions.
20. The process defined by claim 19 in which R2 and R3 are each alkyl.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/011,745 USRE30283E (en) | 1973-04-11 | 1979-02-13 | Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions |
Applications Claiming Priority (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US35029573A | 1973-04-11 | 1973-04-11 | |
| US05/386,652 US3996147A (en) | 1971-02-23 | 1973-08-08 | Novel sulfonium corrosion inhibitors in aqueous acid solutions |
| GB4034473A GB1444171A (en) | 1973-04-11 | 1973-08-24 | Sulphonium salt corrosion inhibitors for aqueous acidic metal cleaning solutions rev |
| JP9448173A JPS5630398B2 (en) | 1973-04-11 | 1973-08-24 | |
| NLAANVRAGE7311808,A NL179147C (en) | 1973-04-11 | 1973-08-28 | METHOD FOR PREPARING AN ACID CLEANING SOLUTION |
| DE19732343382 DE2343382A1 (en) | 1973-04-11 | 1973-08-28 | ACID CLEANING SOLUTIONS |
| FR7331070A FR2245781B1 (en) | 1973-04-11 | 1973-08-28 | |
| CA180,820A CA1005737A (en) | 1973-04-11 | 1973-09-12 | Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions |
| CA180,821A CA1011230A (en) | 1973-04-11 | 1973-09-12 | Sulfonium corrosion inhibitors in aqueous acid solutions |
| US06/011,745 USRE30283E (en) | 1973-04-11 | 1979-02-13 | Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions |
Related Parent Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US35029573A Continuation | 1971-02-23 | 1973-04-11 | |
| US05/669,116 Reissue US4101438A (en) | 1973-04-11 | 1976-03-22 | Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USRE30283E true USRE30283E (en) | 1980-05-27 |
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|---|---|---|---|
| US06/011,745 Expired - Lifetime USRE30283E (en) | 1973-04-11 | 1979-02-13 | Sulfonium compounds as corrosion inhibitors in aqueous acidic cleaning solutions |
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| Country | Link |
|---|---|
| US (1) | USRE30283E (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4637899A (en) | 1984-01-30 | 1987-01-20 | Dowell Schlumberger Incorporated | Corrosion inhibitors for cleaning solutions |
| US6274059B1 (en) * | 1994-07-15 | 2001-08-14 | Lam Research Corporation | Method to remove metals in a scrubber |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3996147A (en) * | 1971-02-23 | 1976-12-07 | The Dow Chemical Company | Novel sulfonium corrosion inhibitors in aqueous acid solutions |
-
1979
- 1979-02-13 US US06/011,745 patent/USRE30283E/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3996147A (en) * | 1971-02-23 | 1976-12-07 | The Dow Chemical Company | Novel sulfonium corrosion inhibitors in aqueous acid solutions |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4637899A (en) | 1984-01-30 | 1987-01-20 | Dowell Schlumberger Incorporated | Corrosion inhibitors for cleaning solutions |
| US6274059B1 (en) * | 1994-07-15 | 2001-08-14 | Lam Research Corporation | Method to remove metals in a scrubber |
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