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Publication numberUS3094490 A
Publication typeGrant
Publication dateJun 18, 1963
Filing dateDec 27, 1960
Priority dateDec 27, 1960
Publication numberUS 3094490 A, US 3094490A, US-A-3094490, US3094490 A, US3094490A
InventorsGeorge S Gardner, Frank E Manson, Jr Edgar S Hayman
Original AssigneeAmchem Prod
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Inhibitor composition and method of inhibiting acid attack on metal in the acidizing f wells
US 3094490 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

INHIBITOR CQMPUSITION AND METHOD OF IN- mlTING ACliD ATTACK N METAL N THE ACKDIZING 0F WELLS George S. Gardner, Elkins Park, Frank E. Manson, Lansdale, and Edgar S. Hayrnan, In, Doylestown, Pa, assignors to Amchem Products, Inc, Ambler, Pa, a corporation of Delaware No Drawing. Filed Dec. 27, 1960, Ser. No. 78,316

2 Claims. ((31. 252-149) This invention relates to inhibitor compositions for preventing or greatly minimizing acid attack on metal of corrosive attack of non-oxidizing acids under conditions of high temperature and high acid concentration such as are often encountered in the acidizing of oil wells.

As is Well known in this art, acidizing operations are carried out on both new and used well formations in order to facilitate recovery of the petroleum. The acidizing technique involves the introduction into the well formation of relatively strong acid solutions and this frequently leads to severe attack by the acid components of these solutions on the Well casing and tubing.

Various types of corrosion inhibitors have been incorporated into the acidizing solutions in an efiort to retard or eliminate their attack on the metal surfaces Within the well. Typical examples of such inhibitors are disclosed in United States Patents 1,719,649; 2,510,063; 2,564,759 and 2,75 8,970, the latter three patents all referring to derivatives of rosin amine. However, experience with these inhibitors in well acidizing operations has indicated that, although some degree of protection is afforded, the over-all protection is insufiicient, especially with regard to what is known as pitting attack on the well tubing. Furthermore, a greater trend toward inefiiciency is encountered with these inhibitors with increased temperatures in the well formations and in this connection attention is called to the fact that the temperature in well formations is related proportionally to the depth thereof. For instance, the temperatures encountered at the bottom of a 10,000 ft. well are often found to be in the neighborhood of about 225 to 235 F. whereas in wells of about 15,000 ft. the temperatures encountered are often in the neighborhood of 300 to 350 F. Beyond this, present well technology is toward the exploitation of ever deeper Well formations and this emphasizes the need for highly effective inhibitors which are stable not only in high concentrations of acid but also at elevated temperatures.

In attempting to circumvent the difficulty arising with increase in temperature the art has made use of arsenic base inhibitors. Initially these inhibitors were apparently successful in well acidizing operations, especially where the formation contained no hydrogen sulfide. However, it was soon discovered that the arsenic contaminant, present in the crude petroleum recovered from such operations, poisoned the catalysts employed in subsequent petroleum refinement, and this drawback, together with the toxic nature of arsenical solutions, has led to a virtual abandonment of these inhibitor systems.

With the foregoing in mind the principal objects of the present invention reside in the provision of improved inhibitor compositions for reducing acid attack on metal surfaces as well as in the provision of an improved method of preventing corrosion of metal surfaces which are exposed to the effects of high concentrations of acid at relatively high temperatures such as are encountered in the deeper oil wells.

Another object of the invention is the provision of a method for inhibiting acid attack on the so-called highstrength alloys used in well tubing.

The present invention is based upon the discovery that the corrosive action of non-oxidizing acids on metal sur- 3,094,490 Patented June 18, 1963 mercapto acid compounds which are useful in our imsurfaces. More particularly, it relates to the prevention proved inhibiting admixture are represented by the formula:

where R is a radical selected from the group consisting of phenyl, benzyl, naphthyl and naphthyl methyl and the haloand alkyl-substitution products thereof; and R is selected from the group consisting of hydrogen and lower alkyl.

The organic corrosion inhibitor component which is useful in our improved inhibiting admixture should be selected from the group consisting of (a) products prepared by the condensation of aldehydes such as aldol, acetaldehyde, butyraldehyde, heptaldehyde, furfuraldehyde and henzaldehyde with amines such as alpha-naphthylamine, diphenylguanidine, aniline, o-toluid-ine, and diethylamine (organic corrosion inhibitors of this type are described in US. Pat. 1,719,649 above referred to), and (b) compound represented by the following formulas:

Where R is a radical selected from the group consisting of abietyl, hydroabietyl and dehydroabietyl; X is hydrogen or the radical (CH CH O),,H; Y is CH A; Z is from the group consisting of hydrogen and the radical CH A; A represents alpha-ketonyl groups, 111 is an integer of from 9 to 38; and n is an integer of from 2 to 10. The preparation and/or use of compounds of this latter group are described in United States Patents 2,510,063; 2,564,759 and 2,758,970 above referred to, the disclosures of which patents are incorporated herein by way of reference.

Hereinafter the broad term corrosion inhibitor compound should be interpreted as identifying any product resulting from the processes of the four patents referred to above unless some other meaning is made clear by the context.

The amount of the mercapto acid compound which must be used in conjunction with the corrosion inhibitor compound has been found to lie within the range of 0.03 to 1.0% of the total acid solution. Use of less than about 0.03% by weight of the mercapto acid compound, based on the total volume of acid solution, fails to guard effectively against a pitting type attack. Conversely, use of more than about 1% (weight/volume) of the rnercapto compound does not appear to offer any additional advantages and actually increases the cost of such inhibitor compositions. A preferred range of mercapto acid compound has been found to be 0.08 to 0.2%

v by weight based on the volume of the acid solution,

Typical examples of mercapto acid compounds which have been found suitable for use in the present invention are presented below in Table I, but these compounds are not to be construed as a limitation of the disclosure except as defined by the generic formula:

1 RS?-COOH where R and R1 are as defined above.

TABLE I Compound No. R R1 v om 1-03111 VI 01@ H Cl 1X 3 .115 C1 X C1- H l Cl XI o1- H x11 icm n XIII ol-ouz H XIV (CHa)a-C H XV CHa- 11-0411 XVI U 11 XVII Compound No. R R1 XVIII H XIX CH3 C Hg XXI H XXII CH3 1 Mixed isomers of xylyl mereapto acetic acids.

Insofar as the organic corrosion inhibitor component or components of our improved inhibiting admixtures are concerned we would like to point out that use of these components as disclosed in the patents noted above has become so widely accepted for general inhibiting purposes that any one skilled in this art can easily determine the optimum amount of the compound required for any particular set of operating conditions. Since this will vary within the well accepted knowledge of the art no specific quantity of these compounds is specified for the present invention. The point which is of importance insofar as our invention is concerned arises in connection with the quantity of mercapto acid compound which should be included in the admixture and even as to this component of our admixture only a lower limit of content is of any real importance except insofar as cost may be a factor. Large quantities of the mercapto acid compound do not seem to do any harm but beyond a certain quantity they do not seem to yield any marked advantage. By way of a minimum quantity we have found that it should be at least 0.03% by weight based on the total 'volume of the acid solution employed in the acidizing operation. We have further found that beyond about 1% by weight no marked additional improvement has been noted and, as indicated above, the preferred range from the standpoint of efiiciency with relation to economy is from about 0.08 to 0.2% by weight based on the total volume of acid solution used in the acidizing operation.

In order to demonstrate more fully the improved performance obtained with the compositions of the present invention there are presented below a series of results showing the inhibiting properties of various mercapto acid compounds as used alone, various organic corrosion inhibitor compounds as described above and used alone, as well as mixtures of both of these types of compounds,

' which results are included by way of example and are not intended to be construed as a limitation of this invention. In all of the reported tests it will be noted that N-8O type tubing was utilized since this particular grade, although not the subject of an API composition specification is widely used in the petroleum industry, and is on of the most difficult alloys to protect from corrosive environments since it is particularly susceptible to a pitting type attack.

An acid solution was prepared containing 15% by weight of hydrochloric acid and was used as the corroding medium on sections of N-SO tubing which were exposed thereto for 4-hour periods at temperatures of 250 F. The corrosive effect of this uninhibited solution is recorded below in Table II. Mercapto acid compound was then added to portions of this 15% hydrochloric solution to yield acid solutions containing the amount of mercapto compound indicated in the table. The mercapto compounds referred to in the following tables are all identified by numbers which refer to similar numbers in Table I for identification of these compounds.

A corrosion inhibitor compound, prepared in aceordance with Example I of US. Patent 2,758,970, except that the reaction was carried out with acetone and acetophenone added consecutively in order to obtain the reaction product corresponding to the structure:

where R is as described above, was then admixed with the 15 by weight of hydrochloric acid solution as prepared above to yield an acid solution containing 0.5% by weight of the corrosion inhibitor compound. This acid solution was then used as the corroding medium on sections of N-80 tubing which were exposed thereto for the time and temperature noted above. The results of this test are reported below in Table II.

Various mercapto acid compounds were then added at a level of 0.2% (weight/volume) to the hydrochloric acid solution containing 0.5% (weight/volume) of the organic corrosion inhibitor compound noted above. The resulting corrosion data are recorded below in Table II, where, in addition to the weight loss figures which are calculated on the basis of a 24-hour test, there is also presented a description of the type of corrosive attack observed for each of the test results.

TABLE II [Using 15% (weight/Weight) of hydrochloric acid] Inhibitor employed Corrosion results Percent Mereapto acid Weight loss, organic lbs/itfi/ Pitting corrosion 24 hours inhibitor Compound Percent None 11.10 Severe. None 1.0 10. 30 Do. None 1.0 11.40 Do. None 1.0 10. 50 Do. 0. 5 0. 5 15 Do. 0.5 0.2 0.090 None. 0. 5 0.2 0.125 Do. 0. 5 0.2 0. 096 Do. 0. 5 0. 2 0.132 Do. 0. 5 0. 2 0. 159 D0. 0. 5 0. 2 0. 136 D0. 0. 5 0. 2 0. 114 D0. 0. 5 0. 2 0. 141 D0. 0. 5 0. 2 0.062 7 Do. 0. 5 0.2 0. 056 D0. 0. 5 0.2 0.102 D0. 0. 5 0. 2 0. 060 D0. 0. 5 0. 2 0. 101 D0. 0. 5 0. 2 0. 095 Do. 0. 5 0. 2 0. 120 D0. 0. 5 0. 2 0. 101 D0.

A solution was prepared containing 15% by weight of hydrochloric acid and was used as the corroding medium on sections of N-80 tubing which were exposed thereto for 6 hours at temperatures of 200 F. The

corrosive effect of this uninhibited acid solution is reported below in Table III.

Three mercapto acid compounds, identified by numerals which correspond to similar numerals in Table I, were added at levels of 0.2 and 1% (weight/volume) to a 15% (weight/weight) hydrochloric acid solution. The effect of these compounds on retarding corrosion of N- tubing under the conditions of time and temperature reported immediately above is shown in Table III.

A corrosion inhibitor was prepared by the reaction of 32 parts of orthotoluidine with 32 parts of 37% formaldehyde solution and 38 parts of 20 Baum hydrochloric, and then adding 98 parts of 37% formaldehyde solution to the mixture in accordance with the disclosure of US. Pat. 1,719,649. This corrosion inhibitor compound was then formulated With 15 by weight of hydrochloric acid to a concentration of 1.0% by weight of the corrosion inhibitor. This inhibited acid solution was then used as the corrosive medium in tests to determine the effects thereof on N-80 type tubing exposed thereto at temperatures of 200 F. for 6 hours. The results of this test are reported below in Table III.

Various mercapto compounds from the list in Table I were then added at various percentage levels (weight/ volume) to the hydrochloric acid solution containing organic corrosion inhibitor compound as discussed in the preceding paragraph and the conditions and results of these tests are reported in Table III below:

TABLE III [Using 15% (weight/weight) of hydrochloric acid] Using the same solutions as employed in Table III, a further series of corrosion tests were run wherein the hydrochloric acid solutions were in all cases saturated with hydrogen sulfide gas. The same operating conditions, namely, 6 hours :at a temperature of 200 F. were employed. These results are summarized in Table IV.

TABLE IV [Using 15% (weight/weight) of hydrochloric acid saturated with hydrogen sulfide gas] Inhibitor employed Corrosion results Percent Mereapto acid Weight loss, organic lbs/ftfi/ Iitting corrosion 24 hours inhibitor Compound Percent None 5.26 Severe. None 2. Do. None 3. 48 Do. None 4. 87 Do.

1.0 0. 208 Moderate. 1. 0 0. 109 None. 1.0 0. 113 Do. 1. 0 0. 122 Do. 1.0 0. 083 Do.

A corrosion inhibitor compound such as used in Example I of U.S. Pat. 2,510,063 and which is sold c011 mercially under the trade name Polyrad 1110A 1 by the Hercules Powder Company of Wilmington, Delaware, was formulated With 15% by weight of hydrochloric acid to produce a testing solution containing 1.0% of the corrosion inhibitor compound. This solution was then used as the corrosion medium on N-8O tubing exposed thereto for 4 hours at 250 F. Several of the mercapto acid compounds listed in Table I were then added to portions of this testing solution and the resulting data from these inhibitor compositions as well as from the use of the individual components alone are reported in Table V.

It will be noted from the various corrosion tests reported above that the mercapto acid compounds when used alone exhibit essentially no noticeable inhibiting property, but when these are combined with the corrosion inhibitor compounds as decribed above, improved corrosion protection results not only with respect to the reduced weight loss of the metal but also with respect to an elimination or substantial reduction of the pitting type attack on the metal surfaces. It is thus quite apparent that the inhibitor compositions of this invention are capable of eliminating or substantially retarding the corrosive attack of non-oxidizing acids on metal surfaces even at high temperatures.

It is within the purview of this invention to provide new, concentrated inhibitor formulations containing both the organic corrosion inhibitor compounds and the mercapto acid compounds as described above. These concentrated formulations have been found desirable since they may be supplied directly to the site where they are to be used and simply added to the acidic solutions being employed in the acid-izing operations.

Since both types of these compounds have been found to possess varying degrees of water-solubilityranging from a few tenths of 1 percent or even lower, to as much as essentially complete water-solubility-the method of formulating will depend entirely upon the particular choice of compounds used. For example, where both the corrosion inhibitor compound and the mercapto acid compound possess sufiicient water-solubility in the amounts used, they may simply be blended to form a concentrated inhibitor admixture. However, where one or more of the compounds have limited solubility, or are substantially corrosion inhibitor compounds and the mercapto acid insoluble in water, it has been found most practical and convenient to formulate these compounds into a nonaqueous solution of a non-ionic surface active agent of the polyalkoxylated-alkylated phenol type. It has been found that alkylated phenols containing from 8 to 10 Reputed to be a rosin amineethylene oxide condensation product having 11 total mols of ethylene oxide and 10% free rosin amine D, as sold by the Hercules Powder Company.

8 carbon atoms in the alkyl group and from 7 to as high as 50 mols of ethylene and/ or propylene oxide per mol of the alkyl phenol, provide completely satisfactory sol-ubilizing action for these inhibitor compounds.

Where a concentrated admixture of corrosion inhibitor compound and mercapto acid compound is used, these ingredients should be present in a weight/weight ratio of from 0.05 to 0.5 part of the mercapto acid compound for each part of the corrosion inhibitor compound.

Where the polyalkoxylated-alkylated phenol type surface active agent is employed for solubilizing act-ion, it is preferred that from about 4 to 40% (weight/weight) of this agent be utilized in the concentrated inhibitor formulation. The balance of this formulation, that is from 60 to 96% thereof, then consisting of an admixture of the mercapto acid compound and the corrosion inhibitor com pound within the ratio noted above.

In order to illustrate such concentrated inhibitor formu lations as falling Within this disclosure, there are listed below several preferred formulations which are presented by way of example but are in no way intended to be 4-methylphenylmercapto-acetic acid (Compound No.

IV in Table I) 75 Tergitol NP-44 68 Example IV Parts Corrosion inhibitor compound 4 794 '2-naph-thylmercapto-acetic acid (Compound No.

XVI in Table I) 42 Triton X-305 5 42 }Polyrad 1110A is reputed to contain 11 mols of ethylene oxide per mol of rosin almine D, as sold by the Hercules Powder Company. (See description at top of column 7.)

Reputed to be a condensation product of nonylphenol 33th 15 mols of ethylene oxide as sold by Union Carbide mpany.

f Reputed to be a condensation product of nonylphenol gith 40 mols of ethylene oxide as sold by Union Carbide ompany.

Prepared by reacting 32 parts of o-toluidine with 32 parts of 37% formaldehyde solution and 38 parts of 20 B. hydrochloric acid, and then adding 98 parts of 37% formaldehyde solution to the mixture as disclosed in U.S. Pat. 1,719,649.

Reputed to be a condensation product of octylphenol with 30 mols of ethylene oxide as sold by Rohm & Haas Company.

We claim:

1. A concentrated inhibitor composition consisting essentially of an admixture of organic corrosion inhibitor from the class consisting of (a) organic condensation product resulting from the reaction of aldehyde from the class of aldol, acetaldehyde, butyraldehyde, heptaldehyde, furfuraldehyde and benzaldehyde with amine from the class of alphanaphthylamine, diphenylguanidine, aniline, o-toluidine and diethylamine, and

10 (b) compound selected from the class consisting of: sisting of phenyl, benzyl, naphthyl and naphthyl X methyl and the halo and alleyl substitution products thereof; and R is selected from the group consisting of hydrogen and lower alkyl; the said mercapto acid (011201120) 111 compound being present in a weight/weight ratio of c ,0 from 0.05 to 0.5 part for each part of organic corand rosion inhibitor compound.

2. A composition according to claim 1 containing also a non-aqueous solution of polyalkoxylated-alkylated R2"'N phenol containing from 8 to 10 carbon atoms in the alkyl Z group and from 7 to 50 mols of oxide from the class of ethylene and propylene oxides per mol of the alkyl phenol, the quantity of said solution being from about 4 to 40% (weight/weight) of the composition with the balance being mercapto acid compound plus organic corrosion inhibitor.

where R is a radical selected from the group consisting of abietyl, hydroabietyl and dehydroabietyl;

X is from the group consisting of hydrogen and the radical (CH CH O) H; Y is CI-I A; Z is from the group consisting of hydrogen and the radical CH A; H n in rtadicals fig g g 3 22 z g g i2 5; References Cited in the file of this patent mrsanmergero m 1 M of from 2 to 10, together with mercapto acid com- UNITED STATES PATENTS pound represented by the formula: 1,719,649 Chamberlain et a1. July 2, 1929 R 1,780,594 Lawrence Nov. 4, 1930 4 1,911,446 Grebe et al May 30, 1933 2,510,063 Bried June 6, 1950 H 25 2,564,759 Haggard Aug. 21, 1951 where R is a radical selected from the group con- 2,758,970 Saukaitis et al June 10, 1953

Patent Citations
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US1719649 *Jan 11, 1927Jul 2, 1929Vanderbilt Co R TPickling and cleaning of metal
US1780594 *Oct 9, 1929Nov 4, 1930Grasselli Chemical CoAcid treatment of metal articles
US1911446 *Oct 17, 1932May 30, 1933Dow Chemical CoMethod of treating deep wells
US2510063 *Jul 20, 1948Jun 6, 1950Hercules Powder Co LtdCorrosion inhibitor
US2564759 *Jun 3, 1950Aug 21, 1951Hercules Powder Co LtdCorrosion inhibitor composition
US2758970 *Jun 10, 1953Aug 14, 1956American Chem Paint CoDerivatives of rosin amines
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4110109 *Oct 27, 1977Aug 29, 1978Minnesota Mining And Manufacturing CompanyOxidation inhibition of steel wool in silver recovery
US4459158 *Sep 29, 1982Jul 10, 1984Phillips Petroleum CompanyThioalkanoic acid derivatives
US5071574 *Apr 5, 1990Dec 10, 1991Ceca, S.A.Deoxygenating with hydrogen sulfide in presence of metal salt and oxyalkylated fatty amine
US5411670 *Jul 26, 1993May 2, 1995Halliburton CompanyMethod and composition for protecting metal surfaces from oxidative environments
US5591381 *Apr 6, 1994Jan 7, 1997Halliburton CompanyCorrosion inhibiting compositions and methods
US5976416 *May 13, 1997Nov 2, 1999Halliburton Energy Services, Inc.Corrosion inhibited organic acid compositions and methods
US6525011Sep 18, 2001Feb 25, 2003Halliburton Energy Services, Inc.Methods and acidizing compositions for reducing metal surface corrosion and sulfide precipitation
US7216710Feb 4, 2004May 15, 2007Halliburton Energy Services, Inc.acidizing solution comprises an acid and a corrosion inhibiting compound comprising the reaction product of a thiol compound and an aldehyde compound; acidizing a near well bore region of a subterranean formation
US7994099Apr 14, 2009Aug 9, 2011Haliburton Energy Services, Inc.Corrosion inhibitor compositions comprising an aldehyde and a thiol and/or an amine functionalized ring structure and associated methods
US7994101Dec 12, 2006Aug 9, 2011Halliburton Energy Services, Inc.treating a metal surface with an aqueous solution containing triphenylphosphine, triethylphosphine, or trimethylphosphine; treating subterranean formations, inhibition of metal corrosion in acidic environments; corrosion resistance
US8058211Dec 12, 2007Nov 15, 2011Halliburton Energy Services, Inc.Corrosion inhibitor intensifier compositions and associated methods
US8361937 *Dec 1, 2010Jan 29, 2013Halliburton Energy Services, Inc.Corrosion inhibitor compositions comprising reaction products of aldehydes and amides and related methods
US8404157 *Feb 24, 2010Mar 26, 2013Halliburton Energy Services, Inc.Methods and compositions for inhibiting corrosion
US20110155959 *Feb 24, 2010Jun 30, 2011Cassidy Juanita MMethods and Compositions for Inhibiting Corrosion
US20120142563 *Dec 1, 2010Jun 7, 2012Halliburton Energy Services, Inc.Corrosion Inhibitor Compositions Comprising Reaction Products of Aldehydes and Amides and Related Methods
EP0383499A2 *Feb 9, 1990Aug 22, 1990Petrolite CorporationSuppression of the evolution of hydrogen sulfide gases from petroleum residua
EP0392896A1 *Apr 2, 1990Oct 17, 1990Ceca S.A.Composition and process to reduce the corrosiveness of oxygenised salty solutions by bubbling with acid gases
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WO2010119235A1 *Dec 16, 2009Oct 21, 2010Halliburton Energy Services, Inc.Corrosion inhibitor compositions comprising the reaction product formed from an aldehyde with a thiol and/or an amine functionalized ring structure and associated methods
Classifications
U.S. Classification252/391, 507/934, 507/244, 252/395, 507/246, 510/489, 252/392, 510/261
International ClassificationC09K8/54, C23F11/04
Cooperative ClassificationY10S507/934, C23F11/04, C09K8/54
European ClassificationC09K8/54, C23F11/04