Int.J.Curr.Microbiol.App.Sci (2014) 3(3):

Similar documents
Corrosion Rate Measurement on C-Steel

Corrosion and inhibition of Cu-Zn alloys in NaCl solution by using permanganate and phosphate anions

Corrosion characteristics of mild steel in aqueous solution of formic acid containing some acetic acid

ELECTROCHEMICAL SYNTHESIS OF POLYPYRROLE (PPy) and PPy METAL COMPOSITES ON COPPER and INVESTIGATION OF THEIR ANTICORROSIVE PROPERTIES

Assignments. 1. Prepare Galvanic series for metals and alloys in flowing sea water. Compare this with the series available for stagnant sea water.

IRON CARBONATE SCALE GROWTH AND THE EFFECT OF INHIBITION IN CO 2 CORROSION OF MILD STEEL

CHAPTER 7 STUDIES ON CORROSION RESISTANCE OF STAINLESS STEEL CLADDINGS

International Journal of Advancements in Research & Technology, Volume 3, Issue 7, July-2014 ISSN

Laboratory Experiments in Corrosion Engineering II

Acid Extract of Polyalthia Longifolia as a Green Corrosion Inhibitor for Mild Steel in H 2 SO 4 Solution

CORROSION BEHAVIOR OF TITANIUM METAL IN PRESENCE OF INHIBITED SULFURIC ACID AT 50 o C 1

Effect of Precorrosion and Temperature on the Formation Rate of Iron Carbonate Film

The electrodeposition of Zn-Mo and Zn-Sn-Mo alloys from citrate electrolytes

Electrochemical study on magnesium anodes in NaCl and CaSO 4 Mg(OH) 2 aqueous solutions

Effect of Heat Treatment on the Corrosion Behaviour of GTM- SU-718 Superalloy in NaCl, HCl and H 2 SO 4 environments

CORROSION OF STEEL IN IONIC LIQUIDS

Three-dimensional NiFe Layered Double Hydroxide Film for Highefficiency

METAL FINISHING. (As per revised VTU syllabus: )

INFLUENCE OF MURRAYA KOENIGII (CURRY LEAVES) EXTRACT ON THE CORROSION INHIBITION OF CARBON STEEL IN HCl SOLUTION

Electrolytic deposition of Zn-Mn-Mo alloys from a citrate bath

ACCELERATED CORROSION TESTING OF GALVANIC COUPLES. James F. Dante, Josh Averett, Fritz Friedersdorf, and Christy Vestal

PERFORMANCE ANALYSIS OF BENCHMARK PLANT FOR SELECTIVE LITHIUM RECOVERY FROM SEAWATER

P-6. Optimization of Citric Acid Passivation for Corrosion Resistance of Stainless Steel 440C. Chi Tat Kwok 1,2 and Wen He Ding 1.

Galvanic corrosion evaluation of 6061 aluminum coupled to CVD coated stainless steel Elizabeth Sikora and Barbara Shaw 6/9/2016

Study on the synergistic effects of additives on the copper corrosion inhibitors

Inhibition of copper pitting corrosion in alkaline sulphate media by benzotriazole at elevated temperatures

NACE CORROSION 2008 TEG 096X Symposia - Paper 1421

STAINLESS STEEL SELECTION FOR FLUE GAS DESULFURIZATION EQUIPMENT

Sealing of Hard Chrome Plating

2. Wet Corrosion: Characteristics, Prevention and Corrosion Rate

The influence of Mg 17 Al 12 phase volume fraction on the corrosion behaviour of AZ91 magnesium alloy. Andrzej Kiełbus* and Grzegorz Moskal

COMPARATIVE STUDY ON THE CORROSION RESISTANCE OF Zn- 0.2 Pb AND Zn-0.5 Sb GALVANIZED COATINGS. A. Bakhtiari 1, H.R. Asgari 2.

POLARIZATION MEASUREMENTS UNDER ATMOSPHERIC CONDITIONS USING A KELVIN PROBE AS A REFERENCE ELECTRODE ABSTRACT

Analytical investigation of passive films formed on (UNS N-08028) in Simulated Phosphoric acid at different Temperature

J. Mater. Sci. Technol., 2010, 26(11),

Supporting Information

Intergranular Corrosion (IGC)

Electronic supplementary information. Efficient energy storage capabilities promoted by hierarchically MnCo 2 O 4

Prevention Strategies Design and Coatings

The effect of electroplating of Cr and Sn on corrosion resistance of low carbon steel (CK15)

PVP-Functionalized Nanometer Scale Metal Oxide Coatings for. Cathode Materials: Successful Application to LiMn 2 O 4 Spinel.

Effect of Anodizing Potential on the Surface Morphology and Corrosion Property of AZ31 Magnesium Alloy

STATE OF ILLINOIS WILLIAM G. STRATTON, Governor

Module-13. Corrosion and Degradation of materials

Corrosion properties of Ag-Au-Cu-Pd Title containing indium. Author(s) Hattori, M; Tokizaki, T; Matsumoto, Journal Bulletin of Tokyo Dental College, 5

Tutorial Corrosion II. Electrochemical characterization with EC-Lab techniques

Combinations of alloys and environments subject to dealloying and elements preferentially removed

Effect of Annealing Process on the Corrosion Resistance of Aluminium 7075-T6 Alloy

Inhibition of the Sulfide Induced Pitting of Copper Nickel Alloy using Benzotriazole

LASER SURFACE MELTING OF 17-4 PH PRECIPITATION-HARDENABLE STAINLESS STEEL Paper 1203

Methods of Corrosion Control. Corrosion Control or Corrosion Management?

INVESTIGATION EFFECT OF BENZOTRIAZOLE ON THE CORROSION OF

1. Introduction. Keywords Alloys, Corrosion, Flow, Iron, 90Cu-10Ni alloys, NaCl solution, Iron content. Paper type Research paper

The Evaluation of Corrosion Behavior of AISI 347 Stainless Steel to ASTM A335 Low Alloy Steel Dissimilar Welds

Studies on Alloys and Composites that Undergo Anomalous Codeposition

Corrosion Protect DLC Coating on Steel and Hastelloy

Sensitization & Corrosion Behaviour of Austenitic Stainless Steel 304 & 316

Electrochemistry Written Response

EFFECTS OF HAMMER PEENING AND AGING TREATMENT ON MICROSTRUCTURE, MECHANICAL PROPERTIES AND CORROSION RESISTANCE OF OIL-GRADE ALLOY 718

Electro catalytic amorphous nickel alloy

Corrosion inhibition of aluminum and aluminum silicon alloys in sodium hydroxide solutions by methyl cellulose

CORROSION PROPERTIES OF CERMET COATINGS SPRAYED BY HIGH-VELOCITY OXYGEN-FUEL. Dragos UŢU, Iosif HULKA, Viorel-Aurel ŞERBAN, Hannelore FILIPESCU

U ACHUTHA KINI a, PRAKASH SHETTY b*, S DIVAKAR SHETTY a, ARUN ISLOOR c, RAMADEV HERLE a

What happens if we connect Zn and Pt in HCl solution? Corrosion of platinum (Pt) in HCl. 1. If Zn and Pt are not connected

Optimization of Zinc Phosphating Process using Statistical Tool

Corrosion Behaviour of 18%Ni M250 Grade Maraging Steel under Welded Condition in Hydrochloric Acid Medium

Stress Corrosion Cracking of an Austenitic Stainless Steel in Nitrite-Containing Chloride Solutions

New inhibitors for copper corrosion*

Galvanic Corrosion Prevention Guide for Water Cooling Systems

CORROSION of Metals CORROSION CORROSION. Outline ISSUES TO ADDRESS... Why does corrosion occur? What metals are most likely to corrode?

Threshold Chloride Concentration of Stainless Steels in Simulated Concrete Pore Solution

(a) To find out which is the more reactive metal, zinc or tin, the following experiment could be carried out. piece of zinc shiny surface

Electrodeposition and compositional behaviour of Zn-Ni alloy

LUBRICANT INDUCED METAL CORROSION - AN ELECTROCHEMICAL IMPEDANCE SPECTROSCOPY APPROACH

Available online at ScienceDirect. Procedia Engineering 184 (2017 )

DETECTION OF PITTING CORROSION OF ALUMINIUM ALLOYS BY ACOUSTIC EMISSION TECHNIQUE

Application Note CORR-4

Electrochemical Behavior of Thin Film Analogs of Mg (Zn,Cu,Al) 2

Korkealämpötilaprosessit

SENSORS FOR MANGANESE

Corrosion Control and Cathodic Protection Data Sheet

Effect of Chloride on Localized Corrosion Initiation of Carbon Steel in a CO 2 Aqueous Environment Xin Gao, Bruce Brown, Srdjan Nesic

Corrosion Inhibition Of Mild Steel In Acid Solution By Thiourea- Zn 2+ - L-Alanine System

CO forms CO 2. forms. (a) The coke reacts with the oxygen in the air to form carbon dioxide. C + O 2

Effects of Grain Refinement on the Corrosion Behaviour of Microalloyed Steel in Sulphuric Acid Solutions

Performance Attributes of Organic Corrosion Inhibitors

Protection Effectiveness of Vapor Corrosion Inhibitor VpCI 619 for Corrosion Under Insulation at Elevated Temperatures

A Case Study: Corrosion Failure of Tube Heat Exchanger

Corrosion Properties of Enhanced Duplex Steel UNS S32304

DEVELOPMENT OF ENVIRONMENTALLY FRIENDLY FORMULATION FOR CORROSION RESISTANCE OF GALVANIZED STEEL SHEET

GENARAL INTRODUCTION TO METALLURGY :Std: XI-CHEMISTRY

Journal of Chemical and Pharmaceutical Research, 2014, 6(1): Research Article

The Basics of Dezincification

Corrosion Behavior of Mild Steel in Seawater from Two Different Sites of Kuala Terengganu Coastal Area

ONLINE MONITORING OF CORROSION UNDER CATHODIC PROTECTION CONDITIONS UTILIZING COUPLED MULTIELECTRODE SENSORS

More than just a Zinc Phosphate. Zinc Phosphate ZP 10

Potentiodynamic Studies of Aluminium 2024 Alloy in Different Concentration of Hydrochloric Acid Medium at Laboratory Temperature

The Effect of Cu and Ni on the Structure and Properties of the IMC Formed by the Reaction of Liquid Sn-Cu Based Solders with Cu Substrate

METALS AND THEIR COMPOUNDS

Sodium nitrite as corrosion inhibitor for mild steel in simulated concrete pore solution

Transcription:

ISSN: 2319-7706 Volume 3 Number 3 (2014) pp. 515-526 http://www.ijcmas.com Original Research Article Anti-Corrosive effect of N-[(benzylidene hydrazino)-propyl]- benzotriazole and N-[(4-oxo-2-phenyl-1,3-thiazolidineimino)-propyl]-benzotriazole for admiralty brass in marine environment A.C.Jayasree and R.Ravichandran * 1 Research and Development Centre, Bharathiar University, Coimbatore 641 046, India. 2 Post Graduate & Research Department of Chemistry, Dr.Ambedkar Government Arts College (Autonomous), Chennai 600 039, India *Corresponding author A B S T R A C T K e y w o r d s Admiralty brass, artificial sea water, SEM, BTA derivatives, polarisation. Benzotriazole derivatives, namely N-[(benzylidene hydrazino)-propyl]- benzotriazole(bpbt) and N-[(4-oxo-2-phenyl-1,3-thiazolidineimino)-propyl]- benzotriazole (OPBT) were synthesised and their inhibition behaviour on admiralty brass in artificial sea water were investigated by the weight-loss method and potentiodynamic polarisation methods. Benzotriazole derivatives were found to act as mixed type inhibitors. Of the compounds studied, OPBT exhibited the best performance, giving more than 94% inhibition efficiency in artificial sea water. Solution analysis revealed the dissolution of both copper and zinc occurred in the presence of the inhibitors. The morphology of the brass after corrosion in the presence and absence of the BTA derivatives was examined using scanning electron microscopy (SEM). The percentage composition of the brass surface was analyzed using energy dispersive X-ray analysis (EDAX). Introduction Copper and its alloys are used extensively and successfully in many types of chemical equipment including evaporators, pumps, valves, fans and fractionating columns. Large quantities of pipes made out of copper and copper alloys are used to make condensers and heat exchangers, where fresh or salt water is used for cooling (Quartarone et al., 1998). Brass is susceptible to a corrosion process known as dezincification and this tendency increases with increasing zinc content of the brass, (Shukla and Pitre, 2002). During the past decade, many techniques have been used to minimise the dezincification and corrosion of brass. One of the techniques for minimising corrosion is the use of inhibitors. The effectiveness of the inhibitor varies with its concentration, the corrosive medium and the surface properties of the alloy. Many inhibitors have been used to minimise the corrosion of brass in different media (Elmorsi et al., 1999). 515

Benzotriazole, for example, has been studied and found to have excellent inhibition properties in several corrosive environments, (Al-kharafi et al., 2002). This molecule contains nitrogen atoms and has been found useful in preventing copper staining and tarnishing. The effectiveness of BTA has been related to the formation of a [Cu + BTA - ] n film. The film is considered to be insoluble and polymeric, (Tromans et al., 1997). Bag et al., (1996), investigated the protective action of azole derivatives on the corrosion and dezincification of 70/30 brass in ammonia solution and concluded that the inhibitors could control corrosion. The aim of present investigation was to study the inhibition efficiencies of N- [(benzylidene hydrazino)-propyl]- benzotriazole(bppt) and N-[(4-oxo-2- phenyl-1,3-thiazolidineimino)-propyl]- benzotriazole (OPBT) on the corrosion and dezincification of admiralty brass in artificial sea water. Interest in chloride media relates to the applicability of brass as the tubing material for condensers and heat exchangers in cooling water systems. For the corrosion study, weight-loss, electrochemical tests, such as potentiodynamic polarisation and solution analysis were used. The morphology of the brass surface examined by scanning electron microscopy (SEM) also was considered. The percentage composition of the brass surface was analyzed using energy dispersive X-ray analysis (EDX). Materials and Methods Materials The material used for this study was admiralty brass supplied in the form of sheet and the chemical composition (weight percent) of the admiralty brass was 70.34% Cu, 28.53% Zn, 0.92% Sn, 0.069% Pb, 0.058% Fe and traces of Mn, Ni & As, as analyzed by optical emission spectrophotometry. The artificial seawater was prepared by dissolving the chemicals (23.9849g NaCl, 5.0290 g MgCl 2, 4.0111 g Na 2 SO 4, 1.1409 g CaCl 2, 0.6986g KCl, 0.1722g NaHCO 3, 0.100 g KBr,0.0143 g SrCl 2 and 0.0254 g H 3 BO 3 ) in 1 litre of distilled water [Milero, 1996]. The inhibitors N-[(benzylidene hydrazino)- propyl]-benzotriazole and N-[(4-oxo-2- phenyl-1,3-thiazolidineimino)-propyl]- benzotriazole were synthesized according to the reported procedures (Adesh Dubey et et al.,2011) and their structures are shown in the scheme 1. Synthesis of N-[(benzylidene hydrazino)-propyl]- benzotriazole (BPBT) A mixture of N-(hydrazino propyl)- benzotriazole (2g, 0.01 mol) and benzaldehyde (1.11g, 0.01 mol) in methanol (20 ml) in the presence of a catalytic amount of glacial acetic acid was refluxed for 5.3 hrs. The solvent was removed under reduced pressure to and the resulting crude product was purified by passing it through a chromatographic column packed with silica gel using chloroform: methanol (8:2 v/v) as eluant. Resulting purified product was recrystallized by chloroform to give compound. Synthesis of N-[(4-oxo-2-phenyl-1,3- thiazolidineimino)-propyl]- benzotriazole (OPBT) A mixture of compound N-[(benzylidene hydrazino)-propyl]- benzotriazole(bpbt) (1g, 0.003 mol) and SHCH2COOH(0.331g 0.003 mol) in methanol (20 ml) containing a pinch of anhy. ZnCl2 was first stirred for about 2 hours followed by 516

refluxing on a steam bath for about 6 hrs. The recation mixture was cooled and excess of solvent was evaporated under reduced pressure. The solid crude product was purified by passing it through a chromatographic column packed with silica gel using chloroform: methonal (8:2v/v) as eluant and again purified by recrystallisation from ethanol to give compound N-[(4-oxo-2-phenyl-1,3- thiazolidineimino)-propyl]-benzotriazole. Methods For the weight-loss method, the brass specimens (4 cm x 2.5 cm x 0.2 cm) were abraded with silicon carbide papers (120-1200grit), thoroughly washed with distilled water, degreased with acetone, rinsed with distilled water, dried and weighed. The specimens were immersed in 300 ml of artificial sea water, with and without inhibitors at 30 o C for 45days. N-[(benzylidene hydrazino)-propyl]- benzotriazole (BPPT) N-[(4-oxo-2-phenyl-1,3- thiazolidineimino)-propyl]- benzotriazole(opbt) For electrochemical studies, the working electrode with an area of 1cm 2 was embedded in epoxy resin in a Teflon holder. The electrode was abraded mechanically with silicon carbide papers from 120 to 1200 grit followed by polishing with 5 m diamond paste. The electrode was thoroughly washed with double distilled water, degreased in acetone for 15 minutes using ultrasonic vibration, rinsed with distilled water and dried. The cell assembly consisted of brass as working electrode, a platinum foil as counter electrode and a saturated calomel electrode (SCE) as a reference electrode with a Luggin capillary bridge. Polarization studies were carried out using a Vibrant potentiostat/ galvanostat model No. VSM/CS/30 at a scan rate of 1mV/s.. The working electrode was immersed in artificial sea water (open atmosphere) and allowed to stabilize for 30 minutes (Ravichandran and Rajendran, 2005). In each case a potential of -1500 mv was then applied for 15 minutes to reduce oxides. The cathodic and anodic polarization curves for brass specimen in the test solution with and without inhibitors were recorded between 500 to 500 mv at a scan rate of 1 mv/s. The inhibition efficiencies of the compounds were determined from corrosion current density using the Tafel extrapolation method. During the anodic polarization, metal dissolution takes place releasing considerable amounts of metal ions from the material. Hence, the solutions were analyzed to determine the leaching characteristics of the brass alloys. The solution left after polarization measurement was analyzed for copper and zinc by inductively coupled argon plasmaatomic emission spectroscopy (ICP-AES). 517

Solutions containing the optimum concentration of the inhibitor were chosen and a blank was also analyzed for comparision purposes. The morphology and composition of the brass surface after polarization measurements was analyzed using JOEL R JSM 35C SEM combined EDAX. Results and Discussion Weight-loss method The corrosion rates and inhibition efficiencies of brass with different concentrations of BPBT and OPBT in artificial sea water at room temperature (30 o C) are given in Table 1. The corrosion rate (CR) and percentage inhibition efficiency (IE %) were calculated using the following equation (Fontana, 1987). CR (bl) CR (inh) IE% = x 100 CR (bl) where W is the weight-loss, D is the density, T is the immersion time, A is the area of the specimen and CR (inh) and CR (bl) are the corrosion rate of brass in the presence and absence of inhibitors respectively. The inhibition efficiency increases with increase in concentration of the inhibitors. The maximum IE% of each compound was achieved at 300 ppm, and a further increase in concentration showed only a marginal change in the performance of the inhibitor. The optimum of concentration of the inhibitors was 300 ppm and OPBT was superior to BPBT. Mechanism of corrosion inhibition The dissolution and film formation of brass in artificial sea water takes place via the reactions outlined below. In the initial corrosion stage, zinc forms ZnO as a result of Zn + H 2 O = ZnO + 2H + + 2e - and copper forms Cu 2 O as a result of 2Cu + H 2 O = Cu 2 O + 2H + + 2e - Thus a passive oxide film consisting of both Cu 2 O and ZnO covers the surface. However, CuCl is formed on the surface (in the presence of chloride) by the reaction Cu + + Cl - = CuCl which may ultimately result in the formation of CuCl 2 complex via CuCl + Cl - = CuCl 2 - The effectiveness of BTA derivatives as corrosion inhibitors for brass can be gauged from the electrochemical behaviour of brass in artificial sea water. The nature of the interaction of inhibitor on the metal surface during corrosion inhibition has been deduced in terms of the adsorption characteristics. In most cases the adsorption of inhibitor from the corrosive medium is a quasi-substitution process. Inhibitor (soln) + nh 2 O (ads) = Inhibitor (ads) + H 2 O (soln) The BTA derivatives are chemisorbed on the metal surface and that this chemisorbed layer prevents adsorption of oxygen and oxide formation. The protective film is a 1:1 complex of Cu (I) and BTA. The film is probably polymeric, in which BTA bridges two copper atoms via N 1 and N 3 and the aromatic ring is aligned parallel to the metal surface. Formation Cu (II) complexes also can occur, but they do not be protective. Chadwick et al concluded that zinc is also 518

incorporated into the surface film in significant quantities. BTA derivatives inhibits by a two-fold mechanism. The chemisorbed film has a hydrophobic backbone that limits the transport of hydrated aggressive ions to the metal surface. Once formed, the film stabilized Cu (I) ions by means of an electronic effect, network formation or both. It is well known that the inhibitive action of organic compound containing S, N and/or O is due to the formation of a coordinate type of bond between the metal and the lone pair of electrons present in the additive. The tendency to form coordinate bond and hence the extent of inhibition can be enhanced by increasing the effective electron density at the functional group of the additive. In aromatic or heterocyclic ring compounds, the effective electron density at the functional group can be varied by introducing different substituents in the ring leading to variations of the molecular structure. Based on the results, both BPBT and OPBT showed better inhibition efficiencies, due to the presence of heteroatom such as N, O, S and electrons on aromatic nuclei. When compared to BPBT, OPBT showed highest inhibition efficiency, which may be due to the presence of S atom and high molecular weight and possessed by the OPBT molecule. The higher inhibition efficiency of the organic compounds are due to the basis of donor-acceptor interactions between the electrons of the inhibitor and the vacant d-orbital of copper surface or an interaction of inhibitor with already adsorbed chloride ions. Polarization studies The cathodic and anodic polarization curves of admiralty brass in artificial sea water containing different concentrations of BPBT and OPBT are shown in Figure 1 and 2. It is evident that in the presence of inhibitor, the cathodic and anodic curves were shifted towards noble direction and the shift was found to be dependent on inhibitor concentration. Tables 2 illustrate the corresponding electrochemical parameters. The E corr values were marginally shifted in the presence of BPBT and OPBT, which clearly indicated that the inhibitors control both cathodic and anodic reactions and thus act as mixed type inhibitors. The current density also decreased with increasing concentrations of the inhibitors. The corrosion rates and inhibition efficiencies (Tamilselvi et al., 2003) were calculated from polarization curves using the following equation. CR = 3.27 x 10-3 x I corr x EW I corr _ I corr(inh) IE% = x 100 I corr Where CR is the corrosion rate (mmpy), D is the density (g cm -3 ), EW is the equivalent weight of the specimen, IE is the inhibition efficiency and I corr (inh) and I corr are corrosion current density in the presence and absence of inhibitors respectively. The values of cathodic Tafel slope (b c ) and anodic Tafel slope (b a ) of benzotriazole derivatives are found to change with inhibitor concentration, which clearly indicates that the inhibitors controlled both the reactions. The inhibition efficiency of BPBT and OPBT in artificial sea water attained a maximum value at 300 ppm. D 519

The values of inhibition efficiency increase with increasing concentration of inhibitor, indicating that a higher surface coverage was obtained in the solution with the optimum concentration of inhibitor. The corrosion rate of admiralty brass in artificial sea water was found to be 11.32 x 10-2 mmpy and it was minimized by adding the inhibitors to a lower value of 1.15 x 10-2 mmpy and 0.64 x 10-2 mmpy due to the adsorption of BPBT and OPBT on the metal surface respectively. A comparison of the values of inhibition efficiency obtained by weight loss measurements and polarization studies bring out clearly the fact that there is a fairly good agreement between these values. It is also found that the compounds function more effectively on the corrosion inhibition of admiralty brass in artificial seawater. Accelerated leaching studies (ICP-AES) The results of solution analysis and the corresponding dezincification factor (z) in the presence and absence of benzotriazole derivatives at their optimum concentration level in natural sea water for brass are given in Table 3. The dezincification factor (z) was calculated using the relation. z = ( Zn/Cu ) sol ( Zn/Cu) alloy Where, the ratio (Zn /Cu) sol is determined from solution analysis and ( Zn/Cu) alloy is the ratio of weight-percent in the alloy (Abbas, 1991). Figure 3 represent the effect of inhibitors on the dissolution of brass in natural sea water. From the figure, it can be observed that both copper and zinc were present in the solution whereas in the presence of inhibitors, which are able to minimize the dissolution of both copper and zinc. The data recorded in tables illustrate that the percent inhibition efficiency against the dissolution of zinc was correspondingly high as compared to the dissolution of copper. This indicates the excellent inhibition efficiency of inhibitors to prevent the dezincification of brass in natural sea water, which is also reflected in the values of dezincification factor. Among the inhibitors studied, OPBT shows highest inhibition efficiency in the dissolution of brass in artificial sea water. The percent inhibition efficiency against the dissolution of Zn was correspondingly high i.e. 96.92% can be achieved in the presence of OPBT containing natural sea water for brass, indicating that the preferential dissolution of zinc was almost completely minimized. Surface composition analysis The surface composition (wt.%) of the alloy in the presence and absence of inhibitors after polarization are given in Table 4. In the absence of inhibitors, the % of Cu and Zn are present in the surface were reduced due to the leaching of metal ions in sea water. Moreover, the higher concentration of chloride ions on the surface shows the penetration of Cl ions from the electrolyte. However, in the presence of BPBT and OPBT, the % of Cu & Zn is closer to that of the bulk composition of the alloy. Based on the surface analysis, these inhibitors exhibited excellent inhibition efficiency in sea water. Morphological examinations Figures 4 show SEM photographs of the brass surface in the absence and presence 520

Inhibitor Concentration / ppm Table.1 Inhibition efficiency at different concentrations of BPBT and OPBT on admiralty brass in artificial sea water Inhibitor concentration (ppm) Corrosion rate x 10-2 (mmpy) Blank 11.26 - BPBT 100 4.96 55.95 200 2.87 74.51 300 1.09 90.32 400 1.10 90.23 OPBT 100 4.12 63.41 200 2.02 82.06 300 0.63 94.40 400 0.65 94.23 Inhibition efficiency (%) Table.2 Tafel polarisation parameters for the corrosion of admiralty brass in artificial sea water containing different concentrations of BPBT and OPBT Corrosion E corr -b b c (mv vs. a I /mv (dec) -1 /mv corr Rate SCE) (dec) -1 / A cm -2 / mmpy x 10-2 Blank -314 48 35 8.97 11.32 - BPBT Inhibition Efficiency / % 100-256 57 48 3.72 4.69 58.53 200-235 68 56 2.53 3.19 71.79 300-217 77 62 0.91 1.15 89.85 400-218 76 63 0.93 1.17 89.63 OPBT 100-250 69 54 3.31 4.18 63.10 200-227 74 65 1.92 2.42 78.59 300-206 92 88 0.51 0.64 94.31 400-208 90 86 0.54 0.68 93.38 521

Fig.1 Polarization curves of admiralty brass in artificial sea water containing different concentrations of BPBT Fig.2 Polarization curves of admiralty brass in artificial sea water containing different concentrations of OPBT 522

Fig.3 Concentration of copper and zinc leached out from brass in artificial sea water containing optimum concentration BPBT and OPBT. Table.3 Effect of optimum concentrations of BPBT and OPBT on the dezincification of admiralty brass in artificial sea water. Inhibitors Concentration Cu (10-6 M) Zn (10-6 M) Dezincification factor (z) Percent inhibition Cu Zn (%) (%) Blank 0.703 17.21 60.36 - - BPBT 0.153 1.84 29.65 78.24 89.72 OPBT 0.063 0.53 20.74 91.03 96.92 523

Table.4 Surface composition (%) of admiralty brass in artificial seawater after polarization with optimum concentration of inhibitors Inhibitors Cu / % Zn / % Cl / % Alloy 70.34 28.53 - Blank 64.32 20.19 14.46 BPBT 68.83 27.04 2.98 OPBT 70.14 27.48 1.24 Fig.4 SEM images of admiralty brass in the absence (a) and in the presence of BPBT (b); OPBT(c) of BPBT and OPBT after polarisation in artificial sea water. In the absence of inhibitors, extensive general corrosion occurred. The SEM micrograph of the 524

brass exposed to artificial sea water (Fig. (4a)) showed that the corrosion products covered the metal surface. Examination of the features shown in Figure 4(b) and 4(c) revealed that the specimen immersed in sea water containing additives, the inhibitor molecules adsorbed on the metal surface, thereby forming a compact surface film, which hinders the penetration of aggressive species into the metal surface, attributed to the better corrosion inhibition on the brass. In the presence of BTA derivatives, the corrosion decreased considerably. Conclusions The following conclusions were drawn from the present study: The substituted benzotriazole derivatives (both BPBT and OPBT) showed good inhibition efficiency in artificial sea water. The potentiodynamic polarisation studies showed that the inhibitors were mixedtype for brass in chloride solution. They decreased the anodic reaction rate more strongly than the cathodic reaction rate and rendered the open circuit potential more positive in artificial sea water. The benzotriazole derivatives easily adsorbed onto the brass surface at the corrosion potential and formed a protective complex with the Cu(I) ion, thereby reducing the susceptibility of brass to corrosion. Solution analysis reveals that the BPBT and OPBT were highly effective in preventing the dezincification of brass. SEM studies confirm the presence of protective BTA film on the alloy surface. EDAX analysis clearly proved that the inhibition is due to the formation of an insoluble stable film through the process of complexation of the substituted BTA molecules. Acknowledgement The authors wish to thank UGC, New Delhi for financial support. References Abbas, M. I.,1991, "Effect of temperature on dezincification and electrochemical behaviour of 70-30 brass in sulphuric acid", B. Corr. J., Vol. 26 No. 4, pp. 273-278. Adesh Dubey, S.K. Srivastava and S.D. Srivastava2011. Conventional and microwave assisted synthesis of of 4- oxo-2-substituted aryl -1,3- thiazolidine derivatives of benzotrazole Analele Universit ii din Bucuresti Chimie serie nou, 02, 115. Al-Kharafi, F. M., and Ateya, B. G., 2002, "Effect of sulphides on the electrochemical impedance of copper in benzotriazole-inhibited media", J. Electrochem. Soc., Vol. 149, No. 6, pp. B206-B210. Bag, S. K., Chakraborty, S. B., Roy, A., and Chaudhuri, S.R., 1996, "2- aminobenzimidazole as corrosion inhibitor for 70-30 brass in ammonia", B. Corr. J., Vol. 31, No. 3, pp. 207-212. Elmorsi, M. A., and Hassanein, A. M., 1999, Corrosion inhibition of copper by heterocyclic compounds, Corros. Sci., Vol. 41, pp. 2337-2352. Fontana, M. G., Corrosion Engineering, 3rd Edition, McGraw-Hill Book Company, New York, 1987. Milero, F.J, 1996, Chemical Oceanography, CHC Press. 1996. 525

Ravichandran, R. and Rajendran, N. 2005 Electrochemical behaviour of brass in artificial seawater: effect of organic inhibitors, Appl. Surf. Sci., Vol. 241, pp. 449-458, Shukla, J., and Pitre, K. S., 2002, "Electrochemical behaviour of brass in acid solutions and the inhibitive effect imidazole, Corrosion Review, Vol. 20, No. 3, pp. 217-228. Tamilselvi, S., Raman, V., and Rajendran, N., 2003, Inhibition of mild steel by benzotriazole derivatives, J. Appl. Electrochem., Vol. 33, No. 12, pp. 1175-1182. Tromans, D., and Silva, J. C., 1997, "Anodic behavior of copper in chloride/tolyltriazole and chloride/ benzotriazole solutions", Corrosion, Vol. 53, pp.16-25. Quartarone, G., Moretti, G., Bellomi, T., Capobianco, G., and Zingales, A.,1998, "Using indole to inhibit copper corrosion in aerated 0.5 sulphuric acid", Corrosion, pp.606-618. 526