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Publication numberUS3600321 A
Publication typeGrant
Publication dateAug 17, 1971
Filing dateDec 31, 1968
Priority dateDec 31, 1968
Publication numberUS 3600321 A, US 3600321A, US-A-3600321, US3600321 A, US3600321A
InventorsRobert J Tedeschi, Paul W Natali
Original AssigneeAir Prod & Chem
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Dimethyl formamide-containing corrosion inhibitor
US 3600321 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

United States Patent 3,600,321 DIMETHYL FORMAMIDE-CONTAININ G CORROSION INHIBITOR Robert J. Tedeschi, Whitehouse Station, and Paul W. Natali, Middletown, N.J., assiguors to Air Products and Chemicals, Inc., Allentown, Pa. No Drawing. Filed Dec. 31, 1968, Ser. No. 789,023 Int. Cl. C11d 7/32 US. Cl. 252148 Claims ABSTRACT OF THE DISCLOSURE Aqueous acid solutions are inhibited against corrosion of metals, especially ferrous metals, by incorporation of a corrosion-inhibiting system composed of a combination of l-hexyn-3-ol, 5-decyn-4,7-dio1 and dimethyl formamide.

This invention relates to the inhibition of metal corrosion in acidic solutions and is more particularly concerned with inhibited aqueous acid solutions suitable for the treatment of metals.

Metal cleaning baths and pickling baths generally comprise aqueous solutions of inorganic acids such as sulfuric acid, hydrochloric acid, and phosphoric acid, and are useful in the cleaning and treatment of iron, zinc, ferrous alloys, and the like.

In the use of aqueous acidic baths to treat metals, additives or inhibitors in the baths are desirable to prevent or inhibit corrosion or erosion of the metal surfaces. Similarly, in the field of oil-well acidizing, it is necessary to use inhibitors in order to prevent corrosion of the oil-well equipment by the aqueous acid solutions employed. Various other industrial operations also involve contact between an aqueous acidic solution and a metal, and an inhibitor must be used in order to minimize corrosion and/or consumption of the metal by such contact.

If no corrosion inhibitor is present when the aqueous acidic solution comes into contact with the metal, excessive metal loss, production of undesirable metal surface properties, excessive consumption or loss of acid, and like adverse results will be experienced. Many different types of inhibitors have been proposed, but there has been a continuing search for corrosion inhibitors which can be used effectively in small concentrations, and which are economical to produce, since the use of inhibitors is a necessary expense and it is economically prudent to ke p this expense at a minimum while, at the same time, realizing the desired inhibition of metallic corrosion or consumption. The need is also for corrosion inhibitors which are effective at high temperatures, e.g. 200 F. and above, such as are encountered in various operations involving acidic solutions, particularly oil-well acidizing where higher and higher temperatures are encountered as the well extends further into the earth.

While various corrosion-inhibiting agents have been proposed, all of such agents are not of equal effectiveness and of the many hundreds of agents which have been contemplated, only a few are sufficiently active to be commercially attractive. This is particularly true in the case of high-temperature operations. Some inhibitors which have been proposed are reasonably effective at low and moderate temperatures, but fail completely when high temperatures are encountered.

There has, therefore been a continuing search for more effective inhibitors, or for ways of making a given inhibitor more effective. This search has involved the discovery of combinations of inhibitors which act together to provide an inhibitor system. However, many of these systems involve relatively expensive components so that, while they may be relatively effective in their corrosion-inhibiting activity, there are disadvantages from an economic standpoint, particularly if they have to be used in substantial quantities in order to bring about the desired corrosion-inhibiting activity. Similarly, many of these systems are in effective at elevated temperatures. In particular, there is a need for a corrosion-inhibiting system comprising a plurality of components wherein relatively inexpen-' sive compounds of poor corrosion-inhibiting action can be catalyzed or potentiated by the other component or components of the system so that the combination has a high corrosion-inhibiting activity even at elevated temperatures.

It is accordingly an object of this invention to provide a novel corrosion-inhibiting system involving a combination of agents which is highly effective from the standpoint of corrosion-inhibiting activity and which is also commercially attractive.

It is a further object of this invention to provide a novel corrosion-inhibiting system comprising a combination of agents wherein one agent has a strong potentiating or catalyzing action upon the other agent so that the corrosion-inhibiting effectiveness of the combination is greater than the additive action of the components of the combination.

It is another object of the invention to provide an inhibiting system of this character effective at high temperatures.

In accordance with this invention, it has been discovered that the above and other objects can be achieved by the provision of a corrosion-inhibiting system comprising a combination of 1-hexyn-3-ol, 5-decyn-4,7-diol, and dimethyl formamide. The ratios among the components of the corrosion-inhibiting system may vary, but the best results are obtained with weight ratios of the two acetylenic alcohols to each other ranging between 1:10 and 10:1, preferably between 1:5 and 5:1, and most suitably between 1:2 and 2:1, and with the weight ratios of th combined acetylenic alcohols to the dimethyl formamide ranging between 1:10 and 10:1, preferably between 1:5 and 5 :1, and weight ratios between 1:2 and 2:1 being most preferred.

The inhibitor system of the invention is useful to inhibit corrosion of metal surfaces in contact with aqueous mineral acid solutions, e.g. hydrochloric acid, sulfuric acid and phosphoric acid, for example in the acidizing of oil wells, in electrolytic cleaning baths, and electrolytic refining of metals, as well as in metal cleaning and pickling baths. The use of the inhibitor system of this invention for corrosion inhibition of metals in aqueous mineral acid solutions is advantageous in that the system can be employed over a wide and useful concentration range. A further advantage of this inhibitor system is that it may be used at elevated temperatures to provide. good corrosion inhibition, even when in relatively low concentration.

The most effective amount of the corrosion-inhibiting system to be used in accordance with this invention can vary, depending upon local operation conditions. Thus, the temperature and other characteristics of the acid corrosive system may have a bearing upon the amount of inhibitor to be used. The higher the temperature and/or the higher the acid concentration, the greater is the amount of corrosion inhibitor required to give optimum results. In general, however, it has been found that a concentration of the corrosion-inhibiting system of the invention between 0.01 and 2%, preferably between 0.01% to 1.2%, by weight of the aqueous acidic solution is an effective corrosion-inhibiting concentration, although higher concentrations can be used when conditions make them desirable, with a concentration between 0.05% to 0.75% by weight being of most general use, at elevated temperatures, e.g. in the neighborhood of 200 F. The acidic solution can be dilute or concentrated and can be of any 3 of the concentrations used in treating metals, e.g. ferrous metals, or for operations involving contact of acidic solutions with such metals, e.g. oil-well acidizing, and the like, for example to 80%. In most operations of the character indicated, acid concentrations of -15% by weight are employed, and non-oxidizing inorganic acids are used. However, it is not intended to limit the invention to any specific use of acidic solutions or with respect to any specific metal or acid.

While the inhibitor system of this invention can be prepared from individual quantities of 1-hexyn-3-ol and 5- clecyn-4,7-diol, a particularly advantageous source of these two chemicals is the reaction mixture obtained by the ethynylation of butyraldehyde with acetylene, using the well-known reaction wherein butyraldehyde and acetylene are reacted in the presence of a catalyst in an inert solvent medium, most commonly an ether, the reaction being carried out at various temperatures but which generally lie in the range of 0 to 50 C. This reaction, which was originally proposed by Favorskii, and has been improved upon by several other workers, is well-described in the literature, and reference is made, for example, to the book Acetylenic Compounds by Thomas F. Rutledge (Reinhold Book Corp., 1968), especially pages 146 to 149, and to the footnotes referred to therein. In a typical operation the aldehyde and the acetylene are reacted in an acetal or an ether as the reaction medium at substantially atmospheric pressure at a temperature of to C., using solid KOH as catalyst in amounts which are substantially stoichiometric (usually slightly in excess) with respect to the aldehyde, the acetylene being in excess of the stoichiometric quantity. The thus-produced mixture of l-hexyn-3-ol and 5-decyn-4,7-diol will vary in composition somewhat, depending upon the specific reaction conditions, but the ratio of l-hexyn-3-ol to 5-decyn-4,7- diol usually lies within the range of 5:1 to 1:4, and most commonly is about 1:1 to 2:1. The inert reaction medium is readily separated by distillation, but minor amounts of the solvent, e.g. up to 10% by weight or more, may be present and such presence does not interfere with the activity of the acetylenic hydroxy compounds. The mixture may also contain minor amounts of by-products produced by condensation, aldolization, or other reactions and are also unobjectionable. Such by-products may range up to 10% by weight but are usually less than about 5% by weight.

It will be understood that a reaction mixture of the character indicated is particularly attractive from a commercial standpoint since purification of the product of the ethynylation reaction is not required, yet the important benefits of the combination of 1-hexyn-3-ol with 5-decyn- 4,7-diol in the system of this invention are realized in the critical area of corrosion inhibition, i.e. high acid concentrations and high temperatures.

The following experiments will serve to illustrate the effectiveness of the corrosion-inhibiting system of this invention under severe corrosion conditions encountered in practical application:

The method used to determine the inhibiting properties of the system of the invention employs test specimens or coupons. To prepare the coupons, they are wiped with acetone to remove any residual oils or grease, and pickled for one minute in 10% hydrochloric acid to eliminate any scale and surface film. After pickling, the coupons are dipped in sodium bicarbonate solution, rinsed well in tap water, rinsed in distilled water, and finally dried with acetone. The clean and dry specimens are then weighed to the nearest 0.1 mg. In carrying out the evaluation, hydrochloric acid of 15% by weight concentration is used in order to duplicate oil-well acidizing conditions. The inhibitor system is added to 4 oz. test bottles, 100 ml. of the acid then added to each bottle; and the mixture shaken vigorously. The bottles are suspended in a constant-temperature bath consisting of a bell jar filled with ethylene glycol and equipped with a stirrer. The temperature is regulated to maintain the samples at 200i2 F. The bot- 4 tles are placed in the bath /2 hour before the test coupons are added to insure temperature equilibrium. The weighed coupons, in duplicate, are then supported on glass hooks in the test bottles and the bottles are covered with watch glasses during the testing period of 16 hours. At the end of the testing period, the bottles are removed from the bath, the coupons withdrawn, rinsed with water, sodium bicarbonate solution, distilled water, and dried in acetone, then weighed to measure weight loss. Corrosion-inhibiting properties are conveniently expressed as percent inhibition, using the following formula:

Percent inhibition Wt. loss of blankwt.loss of test coupon 100 Wt. loss of blank When the acid concentration and temperature are such that the blank would be completely consumed by the acid in the absence of an inhibitor, the foregoing formula can be expressed as:

Percent inhibition Original wt. test couponwt. loss of test coupon Original wt. test coupon EXAMPLE Using the test procedure described above, the inhibitor system of the invention was evaluated for tis effectiveness in preventing corrosion of steel, using 1 in. x 2 in. coupons cut from a in. sheet of a mild steel having the follow: ing typical analysis: 0.15% max. carbon, O.300.60% manganese, 0.04% phosphorous, 0.05% sulfur, the balance iron. Each test sample was prepared by adding to the 15 hydrochloric acid equal parts by weight of dimethyl formamide and a mixture comprising l-hexyn- 3-01 and 5-decyn-4,7-diol in a 2:1 weight ratio, the combined dimethyl formamide and acetylenic carbinol-glycol mixture being added in the amount of 0.5% by weight of the acid. Each sample was evaluated for corrosion inhibiting activity in contact with the N- metal coupon. At the same time, a blank test, using the same acid but without any inhibitor, was made. The following results were obtained:

Percent inhibition,

Again using the test procedure described above, the inhibitor system of the invention was evaluated for its effectiveness in preventing corrosion of N-80 grade steel, using coupons cut from actual tubing of the type employed in the oil industry. The coupons are cut from 2 in. seamless tubing and represent a 72 section having an axial dimension of 1.343 in. and a transverse dimension of 1.343 in. N-80 steel is relatively susceptible to acid corrosion and has the following typical analysis: 038% carbon, 1.32% manganese, 0.02% phosphorous, 0.023% sulfur, 0.18% molybdenum, the balance iron. Each test sample was prepared and employed in the manner de scribed in connection with the previous evaluation. The following results were obtained:

. Percent inhibition,

Inhibitor: 16 hrs. Hexynol-l-S-decyn 4,7-diol+dimethyl formamide 99+ None 0 These tests show the positive action of the combination of hexynol, 5-decyn-4,7-diol, and dimethyl formamide, in accordance with this invention in inhibiting metal corrosion of commercial steel samples in an acid solution of high concentration at an elevated temperature only slightly below the boiling point of water, over a prolonged period of time. The results shown in the foregoing test data are obtained when an ethynylation reaction mixture comprising 1-hexyn-3-ol and 5-decyn-4,7-diol of the type described above is employed in combination with the dimethyl formamide. When the formamide is directly added to the acetylenic carbinol-glycol mixture, it is advantageous first to dissolve it in a small amount of water, e.g. a 25% aqueous solution, and then add the solution to the acetylenic alcohols.

It will be apparent that various changes and modifications may be made in the operations described in the foregoing without departing from the scope of the invention as defined in the appended claims. It is intended, therefore, that all matter contained in the above description of the invention shall be interpreted as illustrative only and not as limitative.

We claim:

1. A metal corrosion-inhibitor mixture for use with aqueous mineral acids which consists essentially of 1-hexyn-3-ol, 5-decyn-4,7-diol and dimethyl formamide wherein the acetylenic alcohols are present in the Weight ratio of 1:10 to 10:1 in relation to each other and the acetylenic alcohols are present in combination in the weight ratio of 1:10 and 10:1 in relation to the dimethyl formamide.

2. An inhibitor mixture as defined in claim 1 wherein the acetylenic alcohols are present in combination in the weight ratio of 1:2 to 2:1 in relation to the dimethyl formamide.

3. A corrosion-inhibited mineral acid comprising an aqueous solution of the mineral acid and a small, effective amount of a corrosion-inhibiting mixture consisting essentially of 1-hexyn-3-ol, 5-decyn-4,7-diol and dimethyl formamide wherein the acetylenic alcohols are present in the weight ratio of 1: 10 to 10:1 in relation to each other and the acetylenic alcohols are present in combination in the weight ratio of 1:10 and 10:1 in relation to the dimethyl formamide.

4. A corrosion-inhibited acid as defined in claim 3 wherein the corrosion-inhibiting mixture is present in the amount of 0.01% to 2% by weight.

5. An inhibited mineral acid as defined in claim 4 wherein the acetylenic alcohols are present in combination in the weight ratio of 1:2 to 2:1 in relation to the dimethyl formamide.

References Cited UNITED STATES PATENTS 3,231,507 1/1966 Beale et al. 252146 3,382,179 5/1968 Keeney et al. 252148 3,428,566 2/ 1969 Herman et a1. 252146 OTHER REFERENCES Rutledge, T. F., Acetylenic Compounds, Reinhold Book Corp., 1968.

LEON D. ROSDOL, Primary Examiner A. I. RADY, Assistant Examiner US. Cl. X.R.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3779935 *Jul 12, 1971Dec 18, 1973Exxon Research Engineering CoInhibition of corrosion
US3920566 *Jun 20, 1973Nov 18, 1975Shell Oil CoSelf-neutralizing well acidizing
US4165294 *May 22, 1978Aug 21, 1979Allied Chemical CorporationPhenol-free and chlorinated hydrocarbon-free photoresist stripper comprising surfactant and hydrotropic aromatic sulfonic acids
US4215005 *Jan 30, 1978Jul 29, 1980Allied Chemical CorporationOrganic stripping compositions and method for using same
US8361937Dec 1, 2010Jan 29, 2013Halliburton Energy Services, Inc.Corrosion inhibitor compositions comprising reaction products of aldehydes and amides and related methods
U.S. Classification510/266, 510/505, 252/392, 507/266, 507/244, 507/934, 510/501, 510/267
International ClassificationC11D3/16, C23G3/00, C11D7/32, C23G1/06, C23F11/04
Cooperative ClassificationC11D3/164, Y10S507/934, C11D7/3263, C23G1/06
European ClassificationC11D3/16D, C11D7/32G, C23G1/06