A NOTE ON THE EFFICACY OF ETHYLENEDIAMINETETRA-ACETIC ACID DISODIUM SALT AS A STRIPPING AGENT FOR CORROSION PRODUCTS OF COPPER Khatibul Huda Summary—The efficacy of ethylenediaminetetra-acetic acid disodium salt (EDTANa2) as a stripping agent for the removal of corrosion products of copper has been studied by simulation experiment. Six corrosion products of copper—malachite, nantokite, basic copper (II) chloride, paratacamite, atacamite and brochan-tite—were synthesized. The interaction between the solid metal, corrosion products and EDTANa2 was evaluated by estimating the amount of copper dissolved in the EDTANa2, and calculating the rate of dissolution at various concentrations and time. As Cu- EDTANa2 water-soluble complex EDTANa2 is a good stripping agent for the removal of corrosion products of copper, without affecting the surface of the metallic copper. The rate of dissolution of corrosion products in EDTANa2 depends on the properties and constituents of individual corrosion products and the concentration of EDTANa2. It is concluded from these findings that the whole process is controlled by forces of diffusion. Introduction Corrosion products [1. 2] of copper or copper alloy artifacts can be removed by stripping agents [3]. for example, alkaline Rochelle salt, alkaline glycerol, sodium hexametaphosphate, citric acidthiourea complex, sodium sesquicarbonate and also ethylenediaminetetra-acetic acid disodium salt (EDTANa2) [4-7]. Farnsworth [8] studied the effect of sodium hexametaphosphate on copper metal. A study was conducted by Merk [9] on bronze and its corrosion products, using alkaline glycerol, alkaline Rochelle salt, sodium hexametaphosphate and citric acid, to ascertain the extent of dissolution of the corrosion products as well as the metal by a simulation experiment. Angelucci [10] and Matteini [11] worked on copper metal and its oxide using Rochelle salt. Merk [12] also conducted an experiment using the same reagents as the earlier study [9], with the addition of benzotriazole. Sharma and Kharbade [13] studied the action of sodium hexametaphosphate and tripolyphosphate on copper. Removal of nantokite (Cud) by sodium sesquicarbonate and its efficacy were studied by Organ [14]. The behaviour of alkaline dithionite for the removal of nantokite was also investigated by MacLeod [15] and Fox [16], who reported differing reactivity of the reagent. The present study uses a simulation experiment to study the rate, extent and nature of dissolution of copper from six different corrosion products and metallic copper at different concentrations of EDTANa2 and exposure times. The efficacy of EDTANa2 as a stripping agent has been evaluated by determining the rate and percentage of dissolution of different corrosion products of copper artifacts and metal. The simulation technique has been adopted to avoid any possibility of damage to valuable artifacts during the research trial. Method Graduated glass-stoppered cylinders were labelled for different reaction times, corrosion products and concentrations. Corrosion products and metal (0-4g) were weighed out into the cylinders, using a Metlar analytical balance, and standardized [17. p. 321] ethylenediaminetetra-acetic acid disodium salt solution (100ml) was carefully poured in. The vessels were closed with the glass stoppers and left undisturbed during the entire experimental period. Corrosion products at the bottom of the vessel started to dissolve and slowly mixed to the entire volume of the solution. After the predetermined time-frame of the experiment, each vessel was turned upside down and shaken gently, for homogeneous mixing of the dissolved material, and immediately filtered to remove any suspended and insoluble matter. Filtrates were buffered by acetic acid-acetate buffer to maintain pH5 [17. pp. 263-265]. Absorbance of the buffered dissolved materials was measured in a UV-Vis Hitachi double beam spectrophotometer (Model No. 210), using a blank solution in the reference cell at a wavelength of 745nm. The total quantity of dissolved copper was estimated using a previously prepared calibration curve. The entire experimental procedure was car- ried out for different corrosion products and copper metal with (MM, 0-15M. 0-2M and 0-25M concentrations of EDTANa2 during a time-frame of 30. 60, 120, 360, 720, 1440 and 2880 minutes and at an ambient temperature of 30°C. The experiment was carried out in duplicate. The amount of copper "t' (g) actually present in 0-4g of corrosion products and copper metal was determined according to conventional methods [17. p. 380]. From the experimental and calculated data, various plots were drawn (Figures 1-4) Calculation The rate of dissolution of powdered solid by a liquid reagent may be expressed by the equation [18]: where W is the weight of unreacted solid at time T. A is the surface area. C is the reagent concentration and k is the rate constant. On solving the equation, the rate of dissolution is given by a plot of W vs. T [19]. W can be calculated as: where W0 = amount of corrosion product/metal taken, t = amount of copper in corrosion product/metal and Q = total amount of copper complexed with EDTANa2 during time T. The rate and percentage of copper dissolution are also calculated according to Bond [20]: Results and discussion Ethylenediaminetetra-acetic acid disodium salt is a hexadentate complexing ligand and also a reducing agent. Due to the presence of nitrogen atoms with a loan pair of electrons, it acts as a strong corrosion inhibitor for metals [21. 22]. The rate of dissolution of corrosion products and metal, in the form of powder and fine turnings respectively, in solutions of EDTANa2 in distilled water are shown as plots of W vs. T. The experimental plots of W vs. T of all the experimental corrosion products in various concentrations of the EDTANa2 solution produce non-linear plots. A typical curve is shown in Figure 1. According to Begum et al. [19], this type of non-linear curve indicates that the surface area of Figure 1 W vs. T plot for atacamite at different EDTANa2 concentrations: (a) 0-1M, (bj 0-15M, (c) 0-20M, (d) 0-25M. the corrosion products does not remain constant during dissolution. The dissolution may cause opening of the metallic surface beneath the corrosion layer in an artifact at some point but other sites may remain partially covered with the corrosion product. This discrepancy can be mitigated by selecting a suitable reaction time during conservation treatment. Moreover, the metal surface may not be affected by the EDTANa2 solution, as shown in Figure 2, since the W vs. T curve follows an almost horizontal straight line for copper metal in different concentrations of EDTANa2, indicating almost no reaction at any time. When W is plotted against log T. the results show straight lines for almost all the corrosion products used in the dissolution experiment, in the range of concentrations used. Typical curves are shown in Figure 3. It may be inferred that the surface area changes inversely with time of dissolution. According to North and Pearson [23], release of a quantity (Q) of metal ion is directly proportional to the square root of the exposure time T, i.e., If the dissolution is governed by diffusion Figure 2 W vs. T plot for metallic copper at different EDTANa2 concentrations: (a) 0-1M, (b) 015M, (c) 0-20M. (d) 0-25M. Figure 3 W vs. log T plot for brochantite in different EDTANa2 concentrations: (a) 0-1M, (b) 015M, (c) 0-20M, Id) 0-25M. processes, plots of Q vs. T½ show a linear character [22]. Q vs. T'½ plots for all the corrosion products at different concentrations of EDTANa2 show an almost linear character, indicating that the dissolution phenomenon is driven by the process of diffusion. A typical plot at 0-1M concentration of EDTANa2 is shown in Figure 4. The rate of dissolution calculated according to Bond [20] also indicates that an increase in concentration increases the rate of dissolution for the experimental corrosion products (Table 1). Conclusion • EDTANa2 solution in water is a good stripping agent for the removal of corrosion products of copper and copper alloys without affecting metallic copper. Figure 4 Plot of percentage dissolution of copper vs. T½ at 0-lM EDTANa, concentration: (a) malachite, (b) nantokite, (c) basic copper(II) chloride, (d) paratacamite, (e) atacamite, (f) brochantite, (g) copper metal. Increase of concentration accelerates the elimination of corrosion products without affecting metal. During removal of the corrosion products, surface area change is not homogeneous. The dissolution process is governed by the force of diffusion. Change of surface area of corrosion product is inversely proportional to time. Different corrosion products do not dissolve at the same rate: it depends on the properties and constituents of the corrosion product. Appendix: experimental corrosion product, metal and reagents Malachite (basic copper carbonate) CuCO3-Cu(OH)3, nantokite (copper(I) chloride) CuCl. basic copper(II) chloride Cu(OH)Cl, paratacamite γ-Cu2(OH),Cl, atacamite S-Cu2(OH),Cl, brochantite (basic copper sulphate) CuSO4 . 3Cu(OH)2 were prepared according to standard methods described elsewhere [24—26]. Purity and identification were confirmed by X-ray diffractometry by comparing the d-spacing value of the prepared corrosion product with the JCPDS card file. X-ray diffractograms were taken in a JDX-8P Jeol X-ray diffractometer using nickel filtered CuKα radiation at 30KV and 20mA and at a scanning speed of 2° (26) min~' with a chart speed of 20mm.mirr1. A detector counting rate of 2000cps was employed for good resolution. Copper metal in the form of turnings was obtained from BDH (England). All other reagents were AnalaR (BDH, England) or Extra Pure (Merck, Germany). References 1 GRAEDEL. T.E., NASSAU. K., and FRANEY, J.P., 'Copper patinas formed in the atmosphere—1 Introduction", Corrosion Science 27 (1987) 639-657. 2 SELWYN, L.S., BINME, J.P., LAYER. M.E., and DOWNHAM, D.A., "Outdoor bronze statues analysis of metal and surface samples', Studies in Conservation 41 (1996) 205-228. 3 PLENDERLEITH, H.J., and WERNER, A.E.A., The Conservation of Antiquities and Works of Art, 2nd edn, Oxford University Press, London (1971) 285. 4 NATHAN, C.C., Corrosion Inhibitor, National Association of Corrosion Engineers, Houston, Texas (1977). 5 ODDY, W.A., and HUGHES, M.J., The stabi- Table 1 Comparison of the rate of dissolution of different corrosion products (% min-1) lization of active bronze and iron antiquities by the use of sodium sesquicarbonate". Studies in Conservation 15 (1970) 183-189. 6 AGRAWAL, O.P., 'Conservation of metals— problems and prospects' in Proceeding of Asian Regional Seminar on Conservation of Metals in Humid Climate, Lucknow (1987) 8. 7 RlEDERER, J., Restoration and Presentation. trans. L. STEPHEN. Goethe Institute. Munich (1989)23. 8 FARNSWORTH, M., The use of sodium metaphosphate in cleaning bronzes". Technical Studies in the Field of the Fine Arts 9(1940^1)21-24. 9 MERK. L.E.. "A study of reagents used in the stripping of bronzes'. Studies in Conservation 23(1978) 15-22. 10 ANGELUCCI, S., FIORENTINO. P., KOSINKOVO. J., and MARABELLI. M., 'Pitting corrosion in copper and copper alloys: comparative treatment test'. Studies in Conservation 23 (1978) 147-156. 11 MATTEINI. M.. and MOLES. A., 'Kinetic control of the reactivity of some formulations utilized for the cleaning of bronze works of art' in ICOM Committee for Conservation 6th Triennial Meeting, Ottawa (1981) 81/23/4. 12 MERK. L.E.. 'The effectiveness of benzotriazole in the inhibition of the corrosive behaviour of stripping reagent on bronzes'. Studies in Conservation 26 (1981) 73-76. 13 SHARMA. V.C.. and KHARBADE. B.V.. 'Sodium tripolyphosphate—a safe sequestering agent for the treatment of excavated copper objects". Studies in Conservation 39 (1994) 39^14. 14 ORGAN, R.M.. "Aspects of bronze patina and its treatment". Studies in Conservation 8 (1963) 19. 15 MACL.EOD. I.D.. "Conservation of corroded copper alloys: a comparison of new and traditional methods for removing chloride ions', Studies in Conservation 32 (1987) 25-40. 16 Fox. G.L.. "A note on the use of alkaline dithionite for treating ancient bronze artifacts'. Studies in Conservation 40 (1995) 139-142. 17 BASSET. J., DENNY. R.C.. JEFFREY. G.H.. and MENDHAN, J., Vogel's Textbook of Quantitative Inorganic Analysis, 4th edn. ELBS and Longman. London (1979). 18 HABASHI. F.. Principle of Extractive Metallurgv. Gordon & Breach Science Publishers. New York (1990) 130. 19 BEGUM. D.A.. ISLAM, P.M., and BISWAS, K.R.. "Kinetics of dissolution of lead sulphate from w:aste battery scrap in the form of powder by aqueous triethanolamine". Journal of Bangladesh Chemical Society 3 (1990) 35-43. 20 BOND. G.C.. "Dissolution of metals and alloys. Part I. The dissolution of copper in solution containing persulfate ion', Journal of Chemical Society (1959) 33-38. 21 BREGMAN, J.I., Corrosion Inhibition. Macmillan, New York (1963). 22 AGRAWAL. R.. and NAMBOODHIRI. T.K.G.. "The inhibition of sulphuric acid corrosion of stainless steel by thioureas'. Corrosion Science 30 (1990) 37-52. 23 NORTH, N.A., and PEARSON. C.. "Recent advances in the stabilisation of marine iron' in Conservation of Iron Object Found in a Salty Environment, ed. R.M. ORGAN, M.E. NOSEK and J. LEHMANN, Historical Monuments Documentation Centre. Warsaw (1978) 26. 24 VOGEL, A.I., A Text Book of Practical Organic Chemistry, 3rd edn, ELBS and Longman, London (1971) 190-191. 25 BALL. M.C., and COULTARD, R.F.M., Thermal studies on halides and basic halide of copper'. Journal of American Chemical Societv (1968) 1417-1419. 26 PARKER, G.D., Mellor's Inorganic Chemistry, Longman. London (1961) 396, 659. 661. Author KHATIBUL HLDA is working as a conservation chemist at Bangladesh National Museum. He graduated with Honours and obtained an MSc in chemistry from the University of Rajshahi, Bangladesh. Later he studied for a PhD in chemistry at Dhaka University, Bangladesh. He was trained in conservation science at ICCROM. His principal research interest is the application of complexing ligands for the preservation of metals and alloys. Address: Department of Conservation Laboratory, Bangladesh National Museum, Shahbag, Dhaka 1000, Bangladesh. Resume—On a etudie I'efficacite du sel disodique de I'acide ethylenediamine tetracetique (EDTANa7j en tant qu'agent complexant pour I'elimination des produits de corrosion du cuivre par des experiences de simulation. Six produits de corrosion du cuivre - malachite, nantokite, chlorure de cuivre (II), paratacamite, atacamite, et brochantite - ont ete synthetises. L'interaction entre le metal solide, les produits de corrosion et I'EDTANa, a ete evaluee en estimant la quantite de cuivre dissoute dans I'EDTA et en calculant le taux de dissolution d diverses concentrations et divers temps. Comme le cuivre-EDTA est un complexe soluble dans I'eau, I'EDTA s'avere un bon agent complexant des produits de corrosion du cuivre, sans affecter la surface du cuivre metallique. Le taux de dissolution de produits de corrosion depend des proprietes et des constituants de chacun des produits et de la concentration en EDTANa,. On peut conclure d partir de ces resultats que Vensemble du processus est regi par des forces de diffusion. Zusammenfassung—Die Effektivitat von Ethyiendiamintetraessigsdure-Dinat riumsal(EDTANa^j als Reinigungsmittel :ur Entfernung von Korrosionsprodukten des Kupfers wurde durch Simultanexperimente untersucht, Sechs Korrosionsprodukte des Kupfers - Malachit, Nantokit, basisches Kupfer-fU)-Chlorid, Paratacamit, Atacamit und Brochantit - wurden synthetisiert. Die Wechselwirkung iwischen dem festen Metall. den Korrosionsprodukten und dem EDTANay wurden anhand der Menge des von EDTANa^ komplex-ierten und gelosten Kupfers bestimmt und daraus die Geschwindigkeit der Auflosung bei verschiedenen Kon:entrationen in Abhangigkeit von der Zeit errechnet. Da Cu-EDTANa, ein wasserloslicher Komplex ist, 1st EDTANa^ ein gutes Agens :ur Entfernung von Korrosionsprodukten des Kupfers, ohne daft die Oberflache des Metalls dabei angegriffen wurde. Die Auflosungsrate der Korrosionsprodukte in EDTANa^ hdngt von den ehemischen Eigenschaften der einielnen Korrosionsprodukte und von der Konzentration des EDTANa7 ab. Es wurde daher gefolgert, dafi der Pro:efi durch Diffusionskrdfte kontrolliert wird. Resumen—La eficacia de la sal disodica del dcido etilendiamino tetraacetico (EDTANaj como un agente decapante para remover los productos de corrosion del cobre ha sido estudiada con un experimento de simulation. Se sintetizaron seis productos de corrosion del cobre: malaquita, nantokita, cloruro bdsico de cobre(II), paratacamita, atacamita y brocatita. La interaction entre el metal solido, los productos de corrosion y el EDTANa, se evaluaron estimando la cantidad de cobre disuelto en el EDTANa, y calculando el nivel de disolucion a varias concentraciones y tiempos. Como en el caso del complejo soluble en agua Cu-EDTANa}, el EDTANa^ es un buen agente decapante para remover los productos de corrosion del cobre, sin afectar la superficie de cobre metdlico. El nivel de disolucion de los productos de corrosion en EDTANa, depende de las propiedades y constituyentes de los productos de corrosion individuales y de la concentration del EDTANa^. Se concluye de estos resultados que el proceso completo es controlado par fuerzas de difusion.