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Publication numberUS3281279 A
Publication typeGrant
Publication dateOct 25, 1966
Filing dateOct 28, 1963
Priority dateOct 28, 1963
Publication numberUS 3281279 A, US 3281279A, US-A-3281279, US3281279 A, US3281279A
InventorsHugh F Schaefer
Original AssigneeUnion Carbide Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Corrosion inhibitors
US 3281279 A
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Description  (OCR text may contain errors)

United States Patent 3,281,279 CORROSION INHIBITORS Hugh F. Schaefer, Lakewood, Ohio, assignor to Union Carbide Corporation, a corporation of New York No Drawing. Filed Oct. 28, 1963, Ser. No. 319,566 7 Claims. (Cl. 136107) This invention relates to the inhibition of corrosion of zinc and it more particularly refers to the inhibition of corrosion of zinc in alkaline environment and to the prevention of the formation of excessive amounts of gas in an alkaline galvanic cell.

Zinc has been the most common anode material for galvanic cells for many years. In the past few years galvanic cells which utilize "an alkaline electrolyte have gained prominence for many applications. It has been found that there is a certain amount of corrosion of the zinc anode in these cells which is not productive of useful electric power. Very often this corrosion occurs when the cell is in storage, and this, of course, tends to reduce the effective life of the cell when it is finally put in service.

A solution has been proposed for this problem which is based upon the saturation or near saturation of the electrolyte with products of zinc corrosion thus putting the system in equilibrium with respect to zinc corrosion. This has been accomplished by adding zinc oxide or zincate ions to the electrolyte. It has also been found that the amalgamation of the Zinc anode very often aids in the inhibition of non-productive corrosion by electrolyte. These proposals have worked well; however, it is desirable to have alternate materials which are effective by themselves to inhibit zinc corrosion.

It is a primary object of this invention to provide materials which inhibit the corrosion of zinc in alkaline environment.

It is another primary object to prevent the formation of large volumes of gas within a zinc cell and thus preserve the str-uctural integrity of the cell.

It is a more particular object to inhibit the non-productive corrosion of zinc anodes in alkaline galvanic cells.

It is another object to improve the characteristics of alkaline galvanic cells having zinc anodes.

This invention is based upon the discovery that there are certain organic compounds which prevent the corrosion of zinc in alkaline environment without relying on the establishment of equilibrium conditions between zinc, alkali, and zinc corrosion products.

In accordance with this invention and the above stated objects, the inhibition of the corrosion of zinc is accomplished by the presence of an inhibiting amount of benzyl tertb-utanol. This compound is characterized by the fact that it is: substantially passive to the electrochemical reaction between zinc and an alkaline environment, chemically inert to both zinc and the alkaline environment and resistance to oxidation.

It has been found that this compound inhibits the corrosion of zinc in both the solid form and in the powdered form. This inhibitor does not interefere with the normal operation of the zinc as an electrode and yet is effective to inhibit non-productive corrosion of the zinc, and to reduce gassing associated therewith.

The term corrosion, refers to non-productive corrosion of the zinc anode which does not produce a usable galvanic current, unless otherwise indicated.


The above described corrosion inhibitor is effective when used with both amalgamated zinc and non-amalgamated zinc. The corrosion of amalgamated zinc, which is normally less subject to corrosion than non-amalgamated zinc, is inhibited to a greater degree by the presence of the herein described inhibitor. The corrosion inhibiting character of benzyl tert-butanol has been found to be substantially stable and does not diminish appreciably with the passage of time under normal storage and operating conditions.

The inhibitor compound can be incorporated in the cell in several ways. For example, the selected inhibitor can be added directly to the electrolyte prior to gelling the electrolyte. Alternatively, the inhibitor can be added directly to the anode material. For example, the inhibitor can be dissolved in a suitable solvent, e.g., acetone, and the powdered zinc anode material then soaked in the solution. The solvent is then evaporated and the treated zinc incorporated in the cell. As another method the inhibitor solution can be sprayed into the anode material. For use in galvanic cells it is preferred to add the corrosion inhibitor to the anode material. In any event a homogeneous distribution of the inhibitor is desirable to provide uniform protection.

The compound described is employed in an inhibiting amount, that is, an amount which is sufiicient to inhibit or substantially prevent the occurrence of non-productive corrosion and formation gas. In general, amounts of about 0.01 to about 1.0 weight percent based on the weight of anode material to be protected, i.e., on the weight of zinc, provide satisfactory corrosion inhibition. The actual amount of inhibitor necessary to provide adequate inhibition in any particular situation can easily be determined by methods well known in the art.

To illustrate the advantageous characteristics of benzyl tert-butanol standard D-size alkaline-manganese dioxide cells were prepared. Powdered zinc, which was amalgamated to the extent of about 4 percent by weight was immersed for about 24 hours in a solution containing one percent benzyl tert-butanol based on the weight of amalgamated Zinc. The solvent was then thoroughly evaporated in a vacuum oven at between 40 C. and 60 C. The treated zinc was then incorporated in standard alkaline-manganese dioxide cells employing potassium hydroxide as the electrolyte.

Table I shows the voltage characteristics of cells containing the treated anodes. Both open circuit potentials and those on a one-ampere load (by the interrupter technique) were observed. Substantially no effect on cell performance was noted.

These cells were then discharged at 0.5 to 1.0 ampere continuous drain to approximately 50 percent of their capacity. Open and closed circuit voltages of the used cells were then recorded. The range of voltages of the treated cells were approximately the same as the ranges observed in control cells, thus again indicating little or no effect of the additives on cell performance. This particular test is believed to be a very severe one in that about percent of control cells, so discharged, showed excessive gassing and, in many cases, actual rupture of the cell containers occurred. After 50 percent discharge,

a series of treated and control cells were connected to mercury manometers to measure gas pressure buildup over a period of 1 to 6 months at ambient room tem- 1.0 weight percent based on the weight of the zinc anode. 7. The galvanic cell described in claim 6 wherein said electrolyte is an aqueous solution of potassium hydroxide and said cathode depolarizer is manganese dioxide.

TAB LE I Voltage of Fresh Cells Voltage of 50 percent Discharged Cells Additive Gassing of 50% Discharged Cells Open Circuit Closed Circuit Open Circuit Closed Circuit (1.0 amp.) (1.0 amp.)

None 1.481.53 1.371.46 1. 241. 28 0.94-1.12 Excessive in majority of cells: cell rupture observed in several cases even after 1 month and particularly after 6 months at ambient room temperature.

Benzyl tert-butanol 1.50 1. 40-1. 43 1. 28-1. 29 1.07-1.15 Substantial reduction of gassing even after six months at ambient room temperature.

What is claimed is:

1. A method of inhibiting corrosion of zinc exposed to an alkaline environment which comprises effecting said exposure in the presence of a corrosion inhibitor comprising benzyl tert-butanol.

2. The method of claim 1 wherein said alkaline environment comprises .01 to 1.0 weight percent, based on the weight of said zinc, of said benzyl tert-butanol.

3. The method of claim 1 wherein said alkaline environment is an aqueous solution of potassium hydroxide.

4. The method of claim 1 wherein said Zinc is amalgamated.

5. A galvanic cell comprising a zinc anode, a cathode depolarizer, an alkaline electrolyte and benzyl tert-butanol in an inhibiting amount.

6. The galvanic cell described in claim 5 wherein the corrosion inhibiting amount is from about 0.01 to about References Cited by the Examiner UNITED STATES PATENTS 2,829,114 4/1958 Hervert 252387 X 2,897,250 7/1959 Klopp 136l07 2,900,434 8/1959 Zimmerman et al. 136l07 X 3,095,331 6/1963 Davis l36l07

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2829114 *May 4, 1955Apr 1, 1958Universal Oil Prod CoCorrosion inhibitor
US2897250 *Mar 27, 1957Jul 28, 1959Mallory & Co Inc P RCorrosion inhibitors for dry cells
US2900434 *Jan 3, 1956Aug 18, 1959Union Carbide CorpCorrosion inhibitors
US3095331 *Feb 10, 1960Jun 25, 1963Ever Ready CoGalvanic cells
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4377625 *Oct 30, 1981Mar 22, 1983Duracell Inc.Corrosion and hydrogen evolution inhibitors for current-producing cells having zinc anodes
U.S. Classification429/347, 429/207, 422/13, 429/230, 252/388
International ClassificationH01M4/62, H01M6/04
Cooperative ClassificationH01M4/628, Y02E60/12, H01M6/04
European ClassificationH01M4/62G, H01M6/04