US665915A - Process of electrolytic production of nickel or allied metals. - Google Patents

Description

UNITED STATES PATENT OFFICE.

MORITZ KUGEL, OF BERLIN, GERMANY.

PROCESS OF ELECTROLYTIC PRODUCTION OF NICKEL OR ALLIED METALS.

SPECIFICATION formingpart of Letters Patent No. 665,915, dated. January 15, 1901.

Application filed March 24, 1900.

To all whom it may concern:

Be it known that I, MORITZ KUGEL, a subject of the King of Prussia, Emperor of Germany, residing at Berlin, Germany, have invented certain new and useful Improvements in Processes for the Electrolytic Production of Nickel or Allied Metals; and I do hereby declare the following to be a full, clear, and eX- act description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.

The usual methods of electrolytically separating nickel from aqueous solutions of its salts do not permit of the production of deposits of more than about one one hundredths of a millimeter in thickness, since with a longer continuance of nickeling the layer formed comes off in thin scales. This disadvantage can be avoided by using a heated electrolyte, as has been long known; but a thick nickel plate thus produced shows a crystalline structure as compared with the rolled nickel of commerce, is very brittle, and is therefore not suited for direct manufacture or technical utilization without being first melted over again.

The object of the present invention is to produce electrolytic nickel in layers of desired thickness in such manner that the prodnot obtained is f ully'equal to rolled nickel as regards its mechanical properties, toughness, firmness, and ductility, and that, therefore, the otherwise necessary process of remelting, rolling, &c., can be omitted. For this purpose any desired nickel-salt solution which by its composition is suited to the electrolytic separation of nickel is provided with an addition of a strong mineral acidwhich will not be changed in its chemical composition by the current-that is to say, the products of decomposition recombine immediately to reconstitute the original material, and a qualitative change of the chemical composition of the bath does not take place. Such an addition of acid ordinarily makes the nickel-bath useless, as it efiects an immediate scaling off of the deposited metal; but if the electrolyte has been preliminarily heated and is kept at a temperature of over 30 centigrade the sealing ofi of the nickel deposit is prevented and an absolutely tough, flexible, and ductile nickel of homogeneous non-crystalline strucberial No. 10,056. (Specimensd ture of any desired thickness can be obtained. The most suitable acids for producing this effect are perchloric acid, perbromic acid, and sulfuric acid. The relative quantity of the addition to be advantageously employed depends upon the temperature and concentration of the bath and also on the desired hardness of the deposit. 7 The proportion ranges, say, between two per cent. and twenty per cent. of that quantity of acid which is contained in the like volume of the simple normal solution. All those acids which are chemically changed by the current and the products of decomposition of which, second arily, by chemical action make the deposit useless are not suited to this process. This isespecially true of nitric acid, the halogen acids, and all organic acids.

In carrying out the process a difficulty is encountered in that with the high temperature of the bath the acidity of the solution is soon diminished if refuge is not taken in the use of very small anodes or insoluble accessory anodes; but both means have the disadvantage, among others, of causing a loss of energy in consequence of the higher current tension which becomes necessary in the bath. The difficulty may be avoided wholly or for the greater part if there be chosen for the electrolyte a highly-concentrated solution of a salt which is formed of the above-named acids and a light metal, such as magnesium,

aluminium, ammonium, sodium, and potassium. In choosing thesalt it is also a condition that it undergoes no chemical change other than that which results in the immediate recombining of its elements during the regular course of the electrolytic process. Combinations of sulfuric acid with potassium or sodium are therefore not well adapted for the purpose, as'during the electrolysis the various possible stages of combination of these salts are formed and reformed in the bath, so that, on the one hand, control of the chemical composition of the bath for the time being is impossible, and, on the other hand, also a steady loss of energy appears in consequence of the reactions. On the other hand, the magnesia salts have proved especially suitable, for even when relatively large anodesurfaces are used these salts make it possible to maintain a uniform acidity of the bath without adding new acids or the like. For instance, in order to make a nickel cliche (which, as is known, possesses the advantage of greater hardness and'durability than the usual copper cliche) according to the process described a solution of nickel sulfate and magnesium sulfate can be used.

The temperature of the solution employed is as high as possible--say 90 to 100 centigrade-because the conductivity increases with the heat, so long as the mold on which the metal is to be deposited is not changed thereby. In molds of easily-fusible materials this heating is naturally not permissible, and a temperature of to 40 centigrade is then suflicient to attain the same eflect on the deposit. The concentration of the solution has no essential influence on the constitution of deposit. Here, too, therefore, one may be guided by a regard for the greatest possible diminution of the bath resistance, and, for example, at 90 centigrade and for one liter of water use eight hundred gramsnickel sulfate and eight hundred grams magnesium sulfate.

The practical acidity of the solution depends in the first place on the quantity of the current. The action of the free acid is shown first by the appearance of a brisk development of the hydrogen at the cathode. If the quantity of the current be too high, with a high acidity, the development of gas may become so violent that the purely mechanical effect of the same becomes detrimental to the deposit. It is practical, therefore, when there is great acidity to choose a somewhat low current. The current may, however,-without harm to the deposit be used essentially stronger than is usual in nickeling-that is, up to ten to twenty amperesper square decimeter-a correspondingly lively movement of the electrolyte in order to mix well being of course necessary.

The process may be used not only for nickel, but also for allied metals-cobalt, for instance. Similarlyit is possible without difii- .culties to separate other metals also, as copper and zinc, together with the nickel, and

thus to produce white-metal by the galvanic method, which is also thoroughly tough and flexible. Thus what is true for nickel and allied metals is true also for the alloys of either plates of white-metal or strips of the essary for the constant composition of the bath.

Finally, the process is vsuited also to the electrolytic production of nickel or allied metals from ores or nickel regulus in combination with one of the familiar electrometallurgical processes. For this purpose the nickelous solution is acidulated, heated, and then electrolyzed, and it is of no consequence here whether the nickel regulus serves directly as are anode or the solution is produced by the chemical method and electrolyzed between insoluble electrodes. In any case the process serves to essentially improve the physical properties of the electrolytic nickel produced. Furthermore, the fact is especially noteworthy that the acidulating alone, especially with sulfuric acid, already at times brings about a chemical purification of the solution. Electrolytic nickel frequently contains lead, so that even after the remelting it is useless for many purposes. Free sulfuric acid precipitates the lead already in the solution and therefore prevents the separation of the same at the cathode, and thus improves the electrolytic nickel also in this regard.

I claim as my invention 1. Process for the electrolytic production of tough, rollable nickel and allied metals by subjecting the same to the action of an electric current in an electrolyteflhe temperature of which is over 30centigrade and keeping the electrolyte acid by the addition of a strong mineral acid not changeable by the current.

2. Process for the electrolytic production of tough, rollable nickel and allied metals, consisting in subjecting the same to the action of an electric current, in an electrolyte, the temperature of which is over 30 centigrade, keeping the electrolyte acid by the addition of a strong mineral acid not chemically changeable by the current, and adding a highly-concentrated solution of a light metal salt not changeable by the current, to facilitate the maintenance of a uniform acidity without the addition of more acid, substantially as described.

In testimony whereof I affix my signature in presence of two witnesses.

MORITZ KUGEL.

Witnesses:

MAX. 0. STAEHLER, HENRY HASPER.