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Publication numberUS2297666 A
Publication typeGrant
Publication dateSep 29, 1942
Filing dateMar 9, 1940
Priority dateMar 9, 1940
Publication numberUS 2297666 A, US 2297666A, US-A-2297666, US2297666 A, US2297666A
InventorsAaron Wachter
Original AssigneeShell Dev
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Internal corrosion prevention in conduits
US 2297666 A
Abstract  available in
Images(3)
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Claims  available in
Description  (OCR text may contain errors)

Patented Sept. 29 1942 INTERNAL CORROSION PREVENTION IN CONDUITS Aaron Wachter, San Francisco, Calif., assignor to Shell Development Company, San Francisco, Calif., a corporation of Delaware No Drawing. Application March 9, 1940,

Serial No. 323,237

3 Claims.

This invention relates to a means for preventing internal corrosion and scale formation in pipe lines and the like, particularly those which are used for transporting hydrocarbons, as for example gasoline, and has also been found useful for removing rust, scale, or other corrosion product deposits when such exist as a pre-condition in pipe lines. The invention provides a practical and economical process for preventing the formation of rust internally in vessels which are constructed of steel or iron-containing alloys and which are used in the transportation or storage of fluids which are substantially immiscible with water.

Conditions in pipes used in the transportation of gasoline in particular are usually highly favorable to corrosion, which results in the formation of rust on the inner pipe wall. The two important factors which give rise to this corrosion are water and free oxygen Water is carried into the pipe as entrained droplets and as dissolved water in the gasoline which enters the pipe from sweetening treaters, washers, or the like. This water maintains the inner pipe wall in a substantially wet or moistened condition. Since the gasoline may contain as much as 0.006 wt. per cent or more of free oxygen which was dissolved in it during treating operations or in storage before the gasoline entered the pipe, the basic conditions for the formation of scale and rust on steel pipe will be present. The extent or rate of corrosion is aggravated by the usually rapid flow of the gasoline over the metal surface and by the presence of corrosive constituents in the gasoline or water associated with the gasoline.

It is an object of this invention to provide means whereby such scale and rust formation when occurring only to a minor degree, since it will be prevented, and in the case where such conditions already exist, to expedite the removal of such deleterious material and prevent further formation thereof. A further object of the present invention is to produce a hydrocarbon oil composition, through addition of a relatively small proportion of an aqueous solution of certain inhibitors to that oil, which imparts corrosion resistance to steel or other iron-containing alloys with which it is in contact. Further, it isan object of the present invention to attain these ends by chemical treatment in such a manner that no unfavorable effects upon the non-corroded portions of the pipe line or upon the hydrocarbon oil will be had.

Internal rusting and corrosion in pipe lines used in transportation of hydrocarbon oils, a field wherein economy is a vitally necessary conseriously decreases the volume of liquid which will flow under constant pressure. This decrease in throughput capacity of pipe is brought about by internal rusting, since one volume of iron will increase approximately thirty times in forming rust, with resulting restriction of internal pipe diameter, and further, since the rust scale is rough and irregular and usually grows in the form of blisters or tubercles, with resulting increase of skin friction. Eliminating this internal corrosion results in increased satisfactory operation and life of hydrocarbon oil containers.

According to the present invention, solutions. preferably aqueous, of alkali metal nitrites, particularly sodium nitrite, 'are introduced into the vessel or conduit together with the hydrocarbon oil in controlled amounts and under controlled conditions in order to inhibit corrosion and for- I mation of rust.

It has been found that water-soluble inhibitors other than the alkali metal nitrites which are known to be suitable for inhibition of corrosion in systems with substantially aqueous phase fluids are inapplicable, ineflicient, or impracticable for use in systems with substantially hydrocarbon oils.

In order to determine the practicable limits for use in pipe line practice, numerous experiments were made with representative samples of the commercial finished gasoline and entrained water associated with it which were found to be corroding a pipe line through which the gasoline was passing. Mixtures of the gasoline and of the pipe line water, to which sodium nitrite and sodium hydroxide were added to give aqueous solutions of various concentrations and hydrogen ion concentration (pH), were shaken in contact with weighed pieces of polished steel for a period usually of two weeks. The pH of the water was adjusted at the start of the experiments because it was found to be a critical factor. At the end of the test period, the steel pieces were removed from the test mixture, examined to determine the extent and severity of corrosion, then they were cleaned to remove rust and/or corrosion scale only, and weighed to determine the total weight loss. From the weight difference thus obtained,.the corrosion rate in terms nitrite concentration that will satisfactorily prevent corrosion and rust scaleformation. The redetermined experimentally in each case.

sults are summarized in the following table:

Corrosion NaNO: concentration as wt. per cent of H10 present N From the above results, it will be seen that between 0.04% and 0.06% sodium nitrite concentration a sudden change in the degree of protection afforded occurs. It has also been found that for sodium nitrite at 0.06% concentration, which appears to be the lowest concentration that it is desirable to use, best results are obtained when the pH of the water is held to a minimum value of at least 8, no additional advantage being gained above a pH of 12. A pH of 6 or lower appears to negative the inhibiting action of the sodium nitrite entirely. In practice, the desired pH is maintained when necessary by injecting a water-soluble alkaline compound, as for example sodium hydroxide, into the pipe line along with Inches/year 0000 inhibitor being introduced into the substantially water-immiscible fluid in the form of an aqueous solution, or as a slurry or paste made by mixing the powdered inhibitor with oil, or as a substantially dry salt bed or cartridge through or over which the whole or a part of the fluid is passed, or in the form of a powder added directly to the gasoline. Further, if desired, the inhibitor may be added in other than aqueous solution, as for example in an alcohol, particularly methyl, or

ether solution or in ammonia or in any other liquid in which the particular alkali metal nitrite to be used is soluble.

The following detailed example is for the purpose of illustrating a mode of executing my invention and the beneficial effects which result from its use. 'It is to be understood that the invention is not to be considered as limited to the specific'modes or conditions of operation disclosed. By a suitable modification of conditions and materials, the inhibition of corrosion also may be achieved. 'Following is a description of an application of my invention to 115 miles of 8- inch' gasoline pipe line.

The new pipe, it was determined, had a 0" factor of 144. At present, pipe line flow efficiency is usually considered in terms of a coefficient C as calculated from the Massachusetts Institute of Technology modification of the Williams and Hazen equation, which is as follows:

' Cdaoapom wherein mechanical cleaning operations gradually to v loosen, remove, and carry 05 the rust scale from the pipe wall, so that a smooth and unrestricted conduit is attained in a relatively shorttime. I believe that the usefulness of the present invention in removing corrosion products results in part from the prevention of additional formation of rust which would tend to cement rust projections or loosened corrosion product particles to the pipe wall, and in part from interaction of the already formed rust with the sodium nitrite.

The quantity of inhibitor used is dependent upon the extent to which it is desired corrosion be decreased, the severity of corrosion encountered, the amounts and kinds of materials present in the hydrocarbon fluid, on the amount of corrosion which has already occurred, and on the rate at which it is desired to remove corrosion product previously formed on the metal walls. Although a concentration of 0.04% by weight sodium nitrite in solution in the aqueous phase has been found to be sufficient for substantially complete inhibition of corrosion under optimum conditions, the preferable concentration for application in actual practice also being dependent upon the factors named above, it may be desirable to employ a higher concentration which can be The quantity of inhibitor present must be suflicient to maintain the concentration of inhibitor at not less than 0.04% by weight in every portion of the aqueous phase which may come into contact with a corrodible metal surface. Preferably a quantity of sodium nitrite amounting to not more intermittent or continuous manner, the corrosion 7 q=flow rate in barrels per hour C=coefiicient d=internal diameter of the pipe line in inches P=friction loss in pounds per square inch per 1000 feet of pipe g=specific gravity of material being transported Gasoline was pumped through this line for a period of seventeen months, at which time the C factor was again determined and found to be .128, indicating a decrease in efficiency of 11.1%

tration of inhibitor to at least 2.0% weight in the total aqueous phase entering the line, and sufficient to amount to 0.000016% (0.16 part per million) by weight of the gasoline entering the pipe line. Sodium hydroxide was also added in sufficient quantities to maintain a pH of 8 to 10 in the aqueous phase. This application of my invention actually amounted to injecting in a continuous manner 5 gallons of 2.5% by weight sodium nitrite solution per 24 hours.

The above treatment was continued for four months, at the end of which period the C factor was again determined and found to be 144; in other words, all of the rust'scale had been removed within this period and the pipe line brought back to its original efliciency. The cost of such treatment at the present price of sodium nitrite (approximately 240 pounds at $0.08 per pound) is negligible, whereas the loss resulting from an 11% decrease in pipe line efliciency is a matter of thousands of dollars for a similar period.

When applying the present method to pipe lines already in a corroded condition, full benefits along the entire length of pipe line cannot be expected immediately following the inception of minimum quantity inhibitor treatment suitable for uncorroded pipe, owing to absorption or reaction of the alkali metal nitrites with constituents of the corrosion product. If it is desirable to obtain com plete cessation of corrosion immediately, it has been found necessary to add further sodium nitrite in quantities sufiicient to react stoichiometrically with said corrosion products, in addition to amounts suflicient to inhibit further corrosion. The amounts of inhibitor necessary must be experimentally determined in each case. Often, however, it is preferable to avoid full immediate attainment of the corrosion inhibitor benefits in a corroded pipe line of long standing, since too rapid release of the large accumulations of corrosion products from the pipe wall may interfere seriously with normal operation of the'pipe line.

tant properties occurs after contact with the inhibitor.

The present process embodies numerous advantages over existing systems for similar use, as for example the cost of sodium nitrite is negligible considering the small quantities necessary for complete corrosion protection, no special or complicated systems for controlling conditions during injection are required, and no after-treat- 4Q her, gum content, or other commercially impormerit of the material in contact with the inhibitor is necessary. Further, contaminants often contained in the hydrocarbon phase, such as complex organic compounds of oxygen, nitrogen, and sulfur, and contaminants contained in the aqueous phase, such as metal salts or compounds en.- trained from sweetening treaters, have little or no effect upon the life or efiicacy of the inhibitor. 1

I claim as my invention:

1. The process of inhibiting internal corrosion in a ferrous metal pipeline carrying light liquid petroleum distillates, comprising subjecting the pipeline to the inhibiting actirn of an aqueous solution of an alkali metal nitrate carried by the said petroleum distillates, the concentration of the alkali metal nitrite being less than 0.01% by weight of the said petroleum distillates in any part of said pipelin and the pH of the alkali metal nitrite solution being in excess .of-6 and not exceeding 12.

2. The process of inhibiting internal corrosion in a ferrous metal pipeline carrying gasoline, comprising subjecting the pipeline to the inhibiting action of an aqueous solution of an alkali metal nitrite carried by the gasoline, the concentration of the alkali metal nitrite being less than 0.01% by weight of the gasoline in any part of said pipeline and the pH of the alkali metal nitrite solution being between 8 and 12. 3. I he process of inhibiting internal corrosion in a ferrous metal pipeline carrying gasoline, comprising subjecting the pipeline to the inhibiting action of an aqueous solution of sodium nitrite carried by the gasoline, the concentration of the sodium nitrite being of the order of 0.16 part per million by weight of the gasoline in any part of said pipeline and the pH of said sodium nitrite solution being between 8 and 12.

inor: wAcn'rEa,

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2419327 *Jun 28, 1943Apr 22, 1947Shell DevCorrosion inhibitors-nitrite salts of secondary amines
US2422515 *Sep 15, 1943Jun 17, 1947Standard Oil CoPrevention of corrosion in ferrous metal pipe lines carrying refined petroleum distillates
US2426317 *Dec 30, 1944Aug 26, 1947Stanolind Oil & Gas CoInhibiting well corrosion
US2426318 *Nov 15, 1945Aug 26, 1947Stanolind Oil & Gas CoInhibiting corrosion
US2436772 *Aug 24, 1945Feb 24, 1948Du PontSolvent for degreasing iron and aluminum
US2457334 *Sep 29, 1944Dec 28, 1948Electrolux AbCorrosion inhibitors in refrigeration system
US2550997 *Feb 14, 1949May 1, 1951Shell DevInhibition of corrosion
US2629649 *Oct 31, 1949Feb 24, 1953Shell DevVapor-phase corrosion inhibitor
US2712363 *May 29, 1951Jul 5, 1955Tide Water Associated Oil CompMinimizing loss of transparency of sight feed lubricator fluids
US2860040 *May 25, 1955Nov 11, 1958Exxon Research Engineering CoPetroleum distillate fuels
US2888338 *Sep 10, 1956May 26, 1959Exxon Research Engineering CoRust inhibited stabilized hydrocarbon fuel oil
US3005780 *Jun 11, 1958Oct 24, 1961Du PontStabilized tetraethyllead antiknock compositions
US3443982 *Jul 1, 1965May 13, 1969Du PontCoatings for rendering corrodible metal corrosion resistant
US4478158 *Apr 29, 1983Oct 23, 1984Eneroil Research Ltd.Condensing furnaces
US4659594 *Sep 1, 1981Apr 21, 1987Phillips Petroleum CompanyEpoxy resin, curing agent, onium salt and hydrocarbon diluent
Classifications
U.S. Classification44/458, 106/14.21, 44/447, 110/343, 44/451, 134/22.13, 134/2, 422/7, 252/387, 106/14.33
International ClassificationC10L1/10, C10L1/12
Cooperative ClassificationC10L1/1266
European ClassificationC10L1/12E