AN ELECTROPLATING METHOD OF FORMING PLATINGS OF NICKEL, COBALT, NICKEL ALLOYS OR COBALT ALLOYS

Abstract: An electroplating method of forming platings of nickel, cobalt, nickel alloys or cobalt alloys with reduced stresses in an electrodepositing bath of the type: Watt's bath, chloride bath or a combination thereof, by employing pulse plating with periodic reverse pulse and a sulfonated naphthalene additive. This method makes it possible to deposit nickel, cobalt, nickel or cobalt platings without internal stresses.

Description: An electroplating method of forming platings of nickel cobalt, nickel alloys or cobalt alloys. Technical Field The present invention relates to an electroplating method of forming platings of nickel, cobalt, nickel alloys or cobalt alloys in an electrodepositing bath of the type: Watt's bath, chloride bath or a combination thereof by employing pulse plating with a periodic reverse pulse. Current density independence is obtained by means of the invention, whereby low internal stresses are always rendered, wherever the measure¬ ment thereof is made on a particular member and whichever current density is used. Background Art The most common electrodepositing baths for nickel electroplating are Watt's baths containing nickel sulfate, nickel chloride and usually boric acid; chloride baths containing nickel chloride and boric acid, and sulf amate baths containing nickel sulfamate, nickel chloride and usually boric acid. The latter baths are used for the more complicated platings and are difficult and comparatively expensive in use. Corresponding platings of cobalt may be formed in similar baths containing cobalt sulfate and cobalt chloride instead of the corresponding nickel salts. By adding other metal salts platings of nickel or cobalt alloys are obtained. It is known to employ a pulsating current, confer for instance W. Kleinekathofer et al, Metalloberfl. 9 (1982), page 411-420, where pulse plating is used by alternating between equal periods of a direct current with a current density of 1 to 20 A/dm 2 and non-current periods, the pulse frequency being from 100 to 500 Hz. By employ¬ ing a pulsating current and as result of the individual current impulses, an increased formation of crystal nucleuses is obtained, thus rendering a more fine-grained and hard plating. It is furthermore known to employ pulse plating with periodic reverse pulse, i.e. alternating between a cathodic and anodic current. In the cathodic current cycle, the desired plating formation is obtained by metal deposition, while a portion of the deposited nickel is removed by dissolution in the anodic current cycle, any nodules in the plating thus being smoothed. In order to ensure that the result is a build-up and not a dissolution of the plating, it is appreciated that the anodic load is to be less than the cathodic load. This method is e.g. described by Sun et al., Metal Fimshing, May, 1979, page 33-38, whereby the highest degree of hardness in the plating is obtained at a ratio between the cathodic and the anodic current density of 1:1 with cathodic cycles T κ of 60 msec, alternating with anodic cycles T A of 20 msec. US patent No. 2,470,775 (Jernstedt et al.) discloses a process for electroplating nickel, cobalt and alloys thereof in an electrodepositing bath containing chlorides and sulfates of the metals. The plating is effected by means of reversed pulse resulting in an improved appearance (smoothness and maximum brightness) as well as in an expedited deposition. An anodic current density is employed of substantially the same range as the cathodic current density. Various additives are mentioned in the US patent, including naphthalene -1,5-disulfonic acid. These additives are referred to as advantageous components, however no directions are rendered in connection with these additives or elsewhere in the patent as to how the mechanical internal stresses are reduced in the platings resulting from electroplating. EP patent No. 0.079.642 (Veco Beheer B.V.) relates to pulse plating with nickel in an electrolytic bath of the Watt's bath type comprising butynediol or ethylene cyanohydrin as brightener. The deposition is preferably performed at a pulsating current without anodic cycles, but it is stated that anodic cycles, i.e. reverse pulse, can also be employed with the same result. It is, however, not possible to use long anodic pulses in a pure Watt's bath without passivating the nickel layer, whereby any further deposition is prevented. Moreover, said patent discloses that the frequen¬ cies used are in a range from 100 to 10,000 Hz. None of the above mentioned publications relate to internal stresses in platings. US patent No. 3,437,568 relates to a method for measuring the internal stresses in electroformed parts, but does not advise how to reduce the internal stresses and does not relate to pulse plating, additives or special nickel baths. DE published specification No. 2.218.967 discloses a bath for electrodeposition of nickel, to which bath a comparatively large amount of sulfonated naphthalene is added, such as from 0.1 mole/1 to saturation so as to reduce the internal stresses in the platings applied by electroplating and with a direct current of e.g. 30 or 60 mA/cm 2 corresponding to 3 to 6 A dm 2 . According to the publication, the internal stresses are only reduced from die undesired tensile stress range to the compressive stress range from 0 to 26,000 psi (approx. 179 MPa) by employing this bath. Usually, the use of said additive only results in a reduction in the stresses in the range from approx. 300 MPa tensile stress to 100 MPa compressive stress and die stress curve is merely moved downward, but is still a function of the current density, which is a normal condition for any type of nickel bath with or without additives. The use of the large amount of additive is, however, also encumbered widi several drawbacks, since the additive is expensive, has detrimental effects on the environ¬ ment and may cause damage to the bath. Thus, an electroplating method, wherein die internal stresses are independent of the current density, cannot be deduced from die teachings of DE 2.218.967. When electroplating members of a simple geometric shape, often comparatively modest variations in the current density occur over different areas of the surface of the members. However, this is not possible when dealing with more complicated geometric shapes, wherein the method according to DE 2.218.967 cannot be employed in practise. Internal mechanical stress is a problem in all nickel and cobalt depositions, even though the process can be controlled satisfactorily in some instances (by means of expensive electrolytes (sulfamate bath), temperature control, concentration, etc.) when dealing with simple geometric shapes. The prior art methods are, however, completely inapplicable for the manufacture of tools for injection moulding, micro mechanical components or similar complicated geometric shapes. Consequently, it is desirable to provide a metiiod, whereby nickel, cobalt, nickel or cobalt alloys can be deposited with substantially reduced or completely widiout internal stresses - even in complicated geometric shapes. It is also desirable diat this result is obtained whichever current density is used for the deposition. Disclosure of the invention The present invention relates to an electroplating method of forming platings of nickel, cobalt, nickel or cobalt alloys in an electrodepositing bath belonging to the type of a Watt's bath, a chloride bath or a combination thereof by employing pulse plating with periodic reverse pulse, said method being characterised in tiiat the electrodepositing bath contains an additive selected among sulfonated naphthalenes. By employing the method according to the invention internal stresses which constitu¬ tes a serious problem can be avoided when forming said platings on geometric shapes of a more complicated structure. Best Mode for Carrying Out the Invention Sulfamate baths are more complicated (difficult and more expensive to maintain), but are generally used to reduce the stress in the platings. However, in a sulfamate bath, it is only possible to obtain platings with satisfactorily low internal mechanical stresses in case of simple geometric shapes. Although sulfamate baths are also used in more complicated geometric shapes, as these present the hitherto best known solution, often the result is not the optimum due to heavy internal stresses in the plating which e.g. may cause deformation or cracks. Sulfamate baths cannot be used for periodic reverse pulse deposition, sulfur alloyed anodes (2% S) being employed to prevent the sulfamate from decomposing in ammoma and sulfiiric acid (ruining the bath). If the current is reversed, the cathode coated with non-sulfur alloyed nickel or cobalt becomes an anode and the sulfamate is destroyed. When using a Watt's bath, a chloride bath or a combination thereof, it is not possible to obtain platings using a direct current without tensile stresses. In sulfama¬ te baths the stress in the plating - from compressive stress through stress-free to tensile stresses - depends on the cathodic current intensity I κ . Consequently, on simple geometric shapes stress-free platings can be obtained by means of a sulfamate bath at a specific I κ which depends on the temperature and may e.g. be of approxi¬ mately 10 A/dm 2 , but on more complicated geometric shapes this current intensity I κ is not distributed evenly on the entire surface of the member and causes internal stresses. The use of the combination according to the invention has surprisingly shown that the internal stresses are very small and independent ofthe cathodic current intensity I κ and thus of the current distribution on the surface. As a result, low internal stresses are obtained wherever on the member the internal stress is measured and independent of the actual local current densities. In this manner, the invention renders it possible to manufacture complicated geome¬ tric shapes completely without or with considerably reduced internal stresses in tiie plating. As additive in the method according to the invention, sulfonated naphthalene is used, i.e. naphthalene sulfonated with from 1 to 8 sulfonic acid groups (- SO 3 H), prefer¬ ably with 2 to 5 sulfonic acid groups, most preferred 2-4 sulfonic acid groups. In practice, a sulfonated naphthalene product usually comprises a mixture of sulfonated naphthalenes with various degrees of sulfonation, i.e. the number of sulfonic acid groups per naphthalene residue. Moreover, several isomeric com¬ pounds may be present for each degree of sulfonation. Typically, the used sulfonated naphthalene sulfonide has a degree of sulfonation on average corresponding to from 2 to 4.5 sulfomc acid groups per molecule, e.g. 2.5- to 3.5 sulfonic acid groups per molecule. In the presently preferred embodiment of the invention, a mixture of sulfonated naphthalenes is used as sulfonated naphthalene additive, said mixture according to analysis containing approximately 90% of naphthalene trisulfonic acid, preferably comprisingnaphthalene-l,3,6-trisulfonicacidandnaphthalene-l,3,7-trisulfonicacid. The naphthalene residue in the sulfonated naphthalene additive is usually free of other substiments than sulfonic acid groups. Any other substiments may, however, be present provided that they are not detrimental to the beneficial effect of the sulfo¬ nated naphthalene additive on minimizing the internal stresses in the plating formed by employing pulse plating. In a particular preferred embodiment according to the invention, the sulfonated naphthalene additive is used in the electroplating bath in the amount of 0.1 to 10 g/1, more preferred in an amount of 0.2 to 7.0 g/1 and most preferred in an amount of 1.0 to 4.0 g/1, e.g. around 3.1 g/1. Moreover, according to the invention the bath composition preferably contains 10- 500 g/1 of NiCl 2 , 0-500 g/1 of NiSO 4 and 10-100 g/1 of H 3 BO 3 , more preferable 100-400 g/1 of NiCl 2 , 0-300 g/1 of NiSO 4 and 30-50 g/1 of H 3 BO 3 and preferable 200-350 g/1 of NiCl 2 , 25- 175 g/1 of NiSO 4 and 35-45 g/1 of H 3 BO 3 , for instance about 300 g/1 of NiCl 2 , 50 g/1 of NiSO 4 and 40 g/1 of H 3 BO 3 . It has proved advantageous that the anodic current density I A is at least 1.5 times the cathodic current density I , more preferable when I A ranges from 1.5 to 5.0 times the I κ and most preferable when I A is 2 to 3 times the I κ . In a preferred embodiment, the method according to the invention may be character¬ ised in that the pulsating current is made up of cathodic cycles, each of a duration T κ of from 2.5 to 2000 msec, and at a cathodic current density I κ of 0.1 to 16 A/dm 2 alternating with anodic cycles, each of a duration of from 0.5 to 80 msec, and at an anodic current density I A of 0.15 to 80 A/dm 2 . A more preferable embodi¬ ment according to the invention is obtained when among the pulse parameters the I κ ranges from 2 to 8 A/dm 2 , the T κ ranges from 30 to 200 msec, the I A ranges from 4 to 24 A/dm 2 and T A ranges from 10 to 40 msec. A particular preferred embodiment is obtained when I κ is from 3 to 6 A/dm 2 , T κ is from 50 to 150 msec. , I A is from 7 to 17 A/dm 2 and T A is from 15 to 30 msec, e.g. when I κ is 4 A/dm 2 , T κ is 100 msec, I A is 10 A/dm 2 and T A is 20 msec. Examples Example 1 A nickel bath containing 300 g/1 of NiCl 2 -6H 2 O and 50 g/1 of NiSO 4 *6H 2 O was admixed, and to which bath 40 g/1 of H 3 BO 3 and 3.1 g/1 of sulfonated naphthalene additive of technical grade comprising 90% naphthalene- 1, 3, 6/7-trisulf onic acid were added. Nickel was deposited on a steel strip fixed in a dilatometer so that the internal stresses in the deposited nickel can be measured as a contraction or a dilation of the steel strip. The temperamre of the bath was 50°C. When nickel was deposited from said bath at a pulsating current having the cathodic pulse of 100 msec, and 3.5 A/dm 2 followed by an anodic pulse of 20 msec and 8.75 A/dm 2 , the internal stresses were measured to be 0 MPa or less than the degree of accuracy of the apparams of approximately ± 10 MPa. Example 2 Following the method according to Example 1 with the exception that only 1.1 g/1 of the same sulfonated naphthalene additive was used, the same result was obtained as in Example 1, i.e. that the internal stresses were to measure to 0 MPa or less than the degree of accuracy of the apparatus of approximately ± 10 MPa. Example 3 Following the method according to Example 2 with the exception that the anodic current density I A and the cathodic current density I κ was set at 1.25 A/dm 2 and 0.5 A/dm 2 respectively, the same result as in Example 1 was obtained, i.e. that the intemal stresses were measured to 0 MPa or less than the degree of accuracy of the apparams of approximately ± 10 MPa. Example 4 Following the method according to Example 3 with the exception that the anodic current density I A and the cathodic current density I κ was set at 18.75 A/dm 2 and 7.5 A/dm 2 respectively, the same result as in Example 1 was obtained, i.e. that the internal stresses were measured to 0 MPa or less than the degree of accuracy of the apparams of approximately ± 10 MPa. Example 5 Using the method according to Example 1, in which the nickel bath containing 300 g/1 of NiCl 2 -6H 2 O and 50 g/1 of NiSO 4 -6H 2 O is substimted by 300 g/1 of CoCl 2 . *6H 2 O and 50 g/1 of CoSO 4 '6H O and the same amount of H 3 BO 3 and sulfonated naphthalene additive, similar cobalt platings can be produced which are expected to have the similar low internal stresses. Example 6 Following the method according to Example 5 with the exception that 1.1 g/1 of sulfonated naphthalene additive was used, similar stress-free cobalt platings may be expected. Example 7 Following the method according to Example 6 with the exception that the anodic current density I A and the cathodic current density I κ was set at 1.25 A/dm 2 and 0.5 A/dm 2 respectively, similar stress-free cobalt platings can be expected. Example 8 Following the method according to Example 7 with the exception that the anodic current density I A and the cathodic current density I κ was set at 18.75 A/dm 2 and 7.5 A/dm 2 respectively, similar stress-free cobalt platings are expected. Comparison Examples Comparison Example 1 Employing the same set-up and materials as in Example 1 , but at a direct current of 4 A/dm 2 , the intemal stresses for comparison with said Example were measured to 377 MPa. Comparison Example 2 Employing the same set-up and materials as in Example 2, but using a direct current of 7.5 A/dm 2 , the intemal stresses were measured to 490 MPa. Comparison Example 3 Employing the same set-up and materials as in Example 2, but instead using a pulsating current without reverse pulse (I κ = 3.5 A/dm 2 , T κ = 100 msec, I A = 0 A dm 2 , T A = 20 msec), the intemal stresses were measured to 410 MPa.

Claims: Claims 1. An electroplating method of forming platings of nickel, cobalt, nickel alloys or cobalt alloys in an electrodepositing bath belonging to the type of Watt's bath, chloride bath or a combination thereof by employing pulse plating with periodic reverse pulse, characterised in that the electrodepositing bath contains sulfonated naphthalene as an additive and that an anodic current density I A at least 1.5 times the cathodic current density I κ is used at the pulse plating. 2. Method according to claim 1, characterised in the use of a sulfonated naphthalene additive in form of sulfonated naphthalene having an average degree of sulfonation of 1 to 6 sulfonic acid groups per naphthalene residue. 3. Method according to claim 2, characterised in that the sulfonated naphthalene additive has an average degree of sulfonation of 2 to 5 sulfonic acid groups per naphthalene residue. 4. Method according to claim 1 for the formation of nickel platings, c h a r a c t- e r i s e d in that the bath composition comprises 10 to 500 g/1 of NiCl 2 , 0 to 500 g/1 of NiSO 4 and 10 to 100 g/1 of H 3 BO 3 , preferably 100 to 400 g/1 of NiCl 2 , 0 to 300 g/1 of NiSO 4 and 30-50 g/1 of H 3 BO 3 , particularly preferable 200 to 350 g/1 of NiCl 2 , 25 to 175 g/1 of NiSO 4 and 35 to 45 g/1 of H 3 BO 3 . 5. Method according to claim 1, characterised in that the anodic current density I A is from 1.5 to 5.0 times the I κ , preferably 2 to 3 times the I κ . 6. Method according to claim 1, characterised in that the pulsating current is made up of cathodic cycles, each of a duration T κ of from 2.5 to 2000 msec at a pulsating or uniform cathodic current density I κ of 0.1-16 A/dm 2 alterna¬ ting with anodic cycles, each of a duration T A of from 0.5 to 80 msec, at an anodic current density I A of 0.15-80 A/dm 2 . 7. Method according to claim 6, characterised in that the pulsating current is made up of cathodic cycles, each of a duration T κ of from 30 to 200 msec, at a cathodic current density I κ of 2-8 A/dm 2 alternating with anodic cycles, each of a duration T A of from 10 to 40 msec, at an anodic current density I A of 5 to 20 A/dm 2 . 8. Pulsating current according to claim 7, characterised in that the pulse parameters I κ , T κ , I A , T A is 4 A/dm 2 , 100 msec, 10 A/dm 2 and 20 msec, respectively. 9. Method according to claim 1, characterised in that the additive is used in the amount of 0.1 to 10 g/1, preferably 0.2 to 7.0 g/1 and particularly 1 to 4 g/1.

Inventors: DYLMER HENRIK, MOELLER PER, TANG PETER TORBEN, DYLMER, HENRIK, MOELLER, PER, TANG, PETER, TORBEN
Applicants: DYLMER HENRIK, MOELLER PER, TANG PETER TORBEN, DYLMER, HENRIK, MOELLER, PER, TANG, PETER, TORBEN
Application year: 1996
Main classification: C25D3
IPC codes: C25D3, C25D5