Electropolishing of silver from cyanide based electrolytes is investigated and reported in this paper. Effect of varyin~ bath ingredients, addition of certain additives, influence of applied voltage resulting current-time behaviour,dissolution rate of silver, surface appearance aDd brightness after treatment etc. are studied in detail to arrive at the optimum composition and operating parameters

Kiruba, D.

Krishnan, R.M.

Sobha , J.

Sriveeraraghavan, S.

IR@CECRI

Builtin ofElectrochemistry 15 (5-6) M~y-June 1l)l}Q, pp 223-227 0256-1 654/l)l)/$ 3-50 © 1l)l}Q CECRI ELECTROPOLISHING OF ELECTROPLATED SILVER SOBHA JAYAKRISHNAN, D KIRUBA, S SRIVEERARAGHAVAN AND RM KRISHNAN Central Electrochemical Research Institute, Karaikudi 630 006. INDIA Electropolishing of silver from cyanide based electrolytes is investiWited and reported in this paper. Effect of varyin~ bath ingredients, addition of certain additives, influence of applit'd volta~e resulting current-time behaviour,dissolution rate of silver, surface appearance aDd brightness after treatment etc. are studied in detail to arrive at the optimum composition and operating parameters. Keywords: Electropolishing, sliver, cyanide based electrolytes INTRODUCTION Electropolishing is an anodic trcatmf'nt method of metals hy which the subm icroscopic, microscopic and macroscopic irregularities on the surface are removed thereby imparting a bright and smooth surface finish. Electropolishing can produce surfaces comparahle to those resulting from huffing at much lower aU 11 ,21· Silver is a precious metal which is electroplate.d for a wide variety of applications, both decorative and functional. The decorative applications of silver are to produce articles of aesthetic appeal like jewellery, medals, cups etc and to coat on food handling hollowware, flatware, forks, spoons etc. The functional applications of silver are to provide surfaces with good bearing properties, high electrical condudivity and umeactive to many common re.agents. When silver is plated for a decorative application it is nt'cessary to get a hright lustrous finish. This may be accomplished either by introducing brighteners in the plating bath or by polishing tbe surface after electroplating. For polishing the plated surface, use of electropolishing is preferred to mechanical polishing as the laller results in higher loss of eastly metal as cQll1part'd to the controlkd removal in the former case. Electropolishing of silver from thiocyanate, thiosulphate. ammoniacal nitrate and cyanide. solutions are mentioned in literature [2-5]. Results of investigation on cyanide based electrolytes arc discussed ill this paper. EXPERIMENTAL Brass panels of 2.5 x 7.5 x 0.03 em were medanically polished and electroplall'd with silver (10 mm) using a strike alld plating schedule as given below: Strike Silver cyanide: 3 g/1; Potassium cyanide: 80 gil; c.d: 1 A/dm2; Anode: Stainless steel; Duration: 30 sec Plating Silver cyanide: 35 gil; Potassium cyanide: 40 gil; Potassium carhonate: 60 gil; .d: 0.5 A/dm 2; Anode: Silver; Duration: 30 mts. !Ulodic tre,atment was carried out by keeping the plated specimt'n as anode in a cell containing the electrolyte under investigation and a ss c.atllOde. The treated surface was observed for brightness visually. Brightness of selected samples wa measured in a reflectivity meter. By weighing the panels before and after treatment the thickness of silver dissolved was calculated. The anodic treatment was carried out under varying conditions of applied voltage and concentration of solution constiluents and the conditions favouring bright polishing detemlined. The current passing through the circuit at varying applied voltages was observed and the stable values of current noted. Under the conditions where wide currenl Ouctuations were observed, current-time behaviour was recorded using a X-I recorder. RESULTS AN)) DISCUSSION Effect of varying KCN concentration It is seen that potassium cyanide is an esse,ntial constituent in produciJlg a hright e.Iectropolished silver surface. When anode trratment is done in the absellCt' of KCN or at 2S gpl, surface appearance is either una ffeeted or brownish film is fonned (Tahle I). This may he due 10 the fonnalion of silver cyanide or oxide 011 the surface which will not dissolve in 223 SOBHA, KIRUBA, SRTVEERARAGHAVAN AND KRISHNAN - Electropolishing of Icctroplated silver TARLE I: Effect of varyin~ KCN concentration Conc of Applied Curr- Surface Dissolu-KCN voltage ent appearance tion rate gil V rnA !lrn/rot a 1.0 10 Brownisb yellow film 0.05 2.0 20 Brown film 0.09 2.5 25 Brown & black film 0.19 3.0 30 Brown & hlack film 0.31 4.0 40 Brown & black film 0.45 25 1.0 50 White 0.56 2.0 75 White 0.86 2.5 80 While 0.90 3.0 80 Brownisb white 1.00 4.0 90 Brown & black fiI!ll 1.10 50 1.0 65 White 0.74 2.0 120 Scmibrigbt 1.50 2.5 130 Brigbt 1.60 3.0 130 Bright 1.60 4.0 144 Brown film 1.66 75 1.0 80 White 0.94 2.0 140 White 2.00 2.5 160 Bright 2.12 3.0 170 Bright 2.20 4.0 190 Brown film 2.25 -.§ 2 E :l. w '<ia:: z Q >­:::J --.J 0 (}) (}) 15 o'--,!;- -.=-~-----____,"*"-----' 50 100 CONCENTRATION OF KCN, g/ I Fig. ]: Influence of KCN concentration on cell current at different applied voltages (I) IV (2) 2V (3) 3V (4) 4V tbe absence of sufficient free ·yanide. At concentrations of 50 gpl and above, bright surface is obtained at applied voltage of 2.5-3.0 V. From this it is dear that enough free cyanide is essential in bringing about dissolution of surface films thereby bringing about polishing. The current passing through the circuit, is (Fig. 1) and the dissolution rate of silver (Fig. 2) are found to increase with increase in KCN concentration. Tbis may be attributed to the increased conductivity of the solution and the ability of KCN. Increase in applied cell voltage also produce.<; increase in Current and dissolution rate. Effect of varying potassium carbonate concentration Though dcctropolishing occurs in the ahsence and at 25 gil ~C03' only semi bright surfaces are obtained (fable 11). At 50 gil concentration and above bright polished surfa{'cs are ohtained at applied voltages of 2.5-3.0 V. This shows that ~C03 controls the dissolution of the film formed on silver surface and improves the surface smoothening effect. However, ~CO~ does not eonlribute substantially towards the dissolution rate (Fig. 3) or the current passing through the circuit (Fig. 4). Effect of varying silver concentration Electropolishing phenomr.non to obtain bright surface appearance occurs even in the absence of silver (fable Ill), but the voltage required is slightly higher (3 V). Bright surfaces are obtained at 3.0-3.5 V at 12.5 gil A N03 concentration. At 25 and 50 gil electropolishing occurs at 2.5- 3.0 V. Reflectivity measurements with the bright surface obtained show values of 85- 90%. Current passing through the circuit and dissolution rate (Figs. 5-6) are found to be 200 <t E >­z ~ 0:: ::J u 100 50 100 Fig. 2: Influence of KeN concentratioin on dissolution rate at different applied voltages (I) IV (2) 2V (3) 3V (4) 4V 224 COt\lC£NTRATJON OF KCN, 9 /I SOBHA, KJRUBA, SRIVEERARAGHAVAN AND KRISHNAN - Electropolishing of electroplated silver TABLE II: Effect of varyin~ Kl-:03 concentration Concn of Applied Current Surface Dissolution Kzr:03 volta~e rnA appearance rate ~I V /-lrn/rnt a	 1.0 50 White 0.40 2.0	 100 White. 1.00 2.5	 110 White 1.30 3.0	 120 Sem ihrigb t 1.40 4.0	 130 Dull 1.46 25	 1.0 60 White 0.60 2.0	 110 White 1.40 2.5	 120 Bright 1.45 3.0	 125 Sl'lll ihrighL 1.50 4.0	 140 Brown film 1.56 50	 1.0 65 WhiLe 0.74 2,0 120 Scm ihrigh L 1.50 25 130 Brighl I.fiO Fig. 4: Influence of KI'Oj cnncenlralir}/1 nn cell currenl at 3.0	 130 Bright 1.60 different ,,!,{,fied voltages (I) I V (2) 2V (3) 3V (4) 1V 4.0	 144 Brown film 1.6fi 75	 1.0 70 White 0.80 Innuence of applied volta~t' on electropolishing 2.0	 130 While 1.54 Tahk IV shows tile rr.lationship betwren applied volLage and 2.5	 135 Bright 1.66 surface appearance. At very low volLages, surface appearance 3.0	 140 Bright 1.66 is almost unafTecLcd. Brightening elTect is Sl'en ahove 2.0 V 4.0	 150 Brown film 1.()8 TARLE 111: Effect of val-ying silvt'r concentration slightly Irs. cr than that in the ahsel1ce of AgNOy This may' Concn of Applied Current Surface Dissolution be tile result of the re.duction in concentralion gradiel1t A~N03 volbge mA appearane rate CONCENTRATION OF K2COJ .g/l Fig. 3: Influence of K2(03 concentraliion on dissn/ution rate at different applied vnlta,::es (I) IV (2) 2V (3) 3V (4) 4V 225 2 3 <l: 2 E ;.-' ~1 0:: 0:: a 50 IOC CONCENTRATION OF K2C03,gll between electrode and bulk olution. 2 ~ E ::L W ~ Z 0 i= ::J 8---' If) 0 50 100 gil V	 /Am / mt o 1.0 75 While 0.80 2.0 130 White UiO 2.5 145 White 1.70 3.0 160 Bright 1.84 4.0 180 Dull white 2.00 125 1.0 70 White 0.80 2.0 12''\ White 1.50 2.5 130 White 1.60 3.0 140 Bright 1.70 4.0 160 Dull white 1.S0 25 1.0 tiS White 0.74 2.0 120 Semibright 1.50 2.5 130 Bright 1.60 3.0 130 Bright 1.60 4.0 144 Brown film 1.66 50 1.0 65 White 0.70 2.0 120 White 1.44 2.5 125 Bright 1.50 3.0 130 BrighL 1.60 4.0 140 Brown film 1.60 SOBHA, KTRUBA, SRfVEERARAGHAVAN AND KRISHNAN - Electropolishing of electroplated silver >--­z w ~ :::J u ,0.. 200­1001­o I I I o	 25 50 CONCENTRATDN OF AgN03 ,gil Fig. 5: Influence of AgN() j coru:entration on cell current at different applied voltuges' (I) IV (2) 2V (3) 3V (4) 4V upto 3.25 V. At still higher cell voltages, brown passive films are observed on the surface. When currenl passing through the circuit was noted at a particular value of applied cell voltage, it is observed that (he currf'nt reaches a high valuc (il)1) and quickly reduccs and attains a stahle. value (is)' The fall in value from illl to is is generally higher at higher voltages. But at the voltages where electropolishing occurs, tbere is a continuous fluctuation III currenL value, the average value is t1ken as is. E E ::J... :w '« 0:: z 31 :::J -'8 o~--.o.o --o-- -----<o- 1 lJ) o °7------:;:l::----------=~---Io	 25 50 CONCENTRATlCN OF AgN03. 9 II Fig. 6: Influence of IIgNO] concentration on dissolution rate at different apl,lied voltuges (I) lV (2) 2V (3) 3V (4) ·IV TABLE TV: Innucne of applied volta~e. Solution compositinn: AgNOJ 25, KeN so, K 2COJ so g/I Applied Current Surface Dissolution voltage V mA appearance rate ,.an/mt 0.25 20 White 0.30 0.50 35 White 0.47 1.00 65 White 0.74 1.50 95 White 1.10 2.00 120 Semibright 1.50 2.25 130 Semibright 1.59 2.50 130 Bright 1.60 2.75 130 Bright 1.60 3.00 130 Bright 1.00 3.25 130 Bright 1.60 3.50 138 Dull while 1.60 3.75 140 Brown film 1.62 4.00 144 Brown film 1.66 4.50 156 Brown film 1.70 5.00 166 Black film 1.76 Current-voltage and dissolution rate-voltage graphs are shown in Fig. 7. It is seen that the current !lowing through the circuit (Curve I) and the dissolution rate remain almost constanL in the ekctropolishing region. This type of a current-voltage curve is Iypical of elcctropolishing systems [6,71 wherein the first rising portion corresponds to metal dissolution, lhe horizontal portion to polishing phenomenon and the nexl rising portion to pilling wilh gas evolution. 'P	 200 «E E ~	 1­W Z'<i	 w a:	 a:a:z	 OJ0	 u is61 100 :2 0 ~----+----+4----+---"O VOLTAGE. V Fig. 7: Influence of applied voltaRe on cell current (curve I) ami dissolution rate (curve 2) Solution concentration: AgNO./ 25, KCN 50, K 2COJ 50 gil 226 SOBHA, KTRUBA, SRfVEERARAGHAVAN AND KRISHNAN - Electropolishing of electroplated silver ~ 1.Ii ?OmA Ii"	 T ":',I 1\ I, <t {I E 1\ .... r,I,:z I \Ii! I Ill: :::> I I U I I ~""----"-_ _, ----------__ 1 I I o 30 60 TIME, sec Fig. 8: Curre1ll vs time graph during anndic treatment at 2V (curve J) and 4V (curve 2) Innuence of applied voltage on current-time curves These experiments were a imed at observing the variation of current with time during tbe anodic Ireatl11t':nl so as to get a further insight into the polishing phenomenon. The resulting graphs are shown in Figs. 8-9. When the anodic treatment was done at 2.0 or 4.0 V (Fig. 8) the resultant current decreases from a maximum value and reaches a stable value. But when the voltage was 2.5 or 3.0 V, tbe resulting i-t graph has the fonn shown in Fig. 9. This type. of curre.nt Ouctuation is indicative of a cydic phenomenon 18] involving the fomlation of a passive film and its dissolution. From this i-t behaviour we can conclude that the polishing action occurs due to a controlled passivation- dissolution mechanism. The passive fillll forllle.d being thicker in rt':cessed areas leads to preferential di solution of projecting areas whereby the surface irregularities arc Tl'lllovcd. CONCLlJ~ION *	 A solution suitahle for electropolishing of r.lectroplated silver has the following composition and operating para meters. T I I o 30 60 TIME ,sec Fig. Q: Current vs time graph during electropolishing at 2.5 V Silver nitrate: 25 gil; Potassium cyanide: 50 gil;* Potassium carbonate: 50 gil; Applied voltage: 2.5-3.0 V; Cathode: ss *	 The mechanism of electropol isbing lhrough the cyclic phenomena of passivalion-dissolution-passivation is verified based on lhe current-lime brhaviour during ele.Clropolishing expe.rimenls. REFERENCES I.	 R Subramanian, Corro' Bull, 3 (1983) 140 2.	 W J M Tegart, The Electrolytic and Chemical Polishing of Metals, Pergamon Pr s (1959) 3, P A Yuzikis, T Y Yankauskas and V A Kaikaris, J Appl Chem USSR, 49 (1976) 2524 4, V N Nikulin and M Z Tsypin,l Appl Chem USSR, 33 (1960) 465 5, P A Yuzikis, T Y Yankauskas and D A Buchinskas,] Appl Chern USSR, 52 (1979) 1577 6, N Sato, K Kudo and T Noda, Corrosion, JO (1974) 237 7.	 D Landolt, Electrochim Acta, 32 (1987) 1 8,	 H T Francis and W H Coiner,] Electrocltem Soc, 97 (I 50) 237 227 

Electropolishing of electroplated silver

Abstract

Similar works

Full text

Available Versions

IR@CECRI