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2-Hydroxyacetophenone-aroyl Hydrazone Derivatives as Corrosion Inhibitors for Copper Diss

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2-Hydroxyacetophenone-aroyl Hydrazone Derivatives as Corrosion Inhibitors for Copper Diss

ution in Nitric Acid Solution

A.S. Fouda,* M.M. Gouda: andS.I.AbdEl-Rahman

ChemistryDepartment, Faculty of Science, El-Mansoura University,El-Mansoura,Egypt

‘ChemistryDepartment, Faculty of Science, El-Menoufia University, El-menoufia, Egypt Received March17, 2000

Theeffect of2-hydroxyacetophenone-aroyl hydrazonederivativeson theinhibition of copper corrosion in 3N nitric acidsolutionat303 K was investigated by galvanostatic polarization and thermometric techniques. A sig­ nificant decreaseinthecorrosion rateof copper wasobservedinthepresence of theinvestigated compounds.

The corrosion rate was found to depend on the nature andconcentrations of the inhibitors.The degree ofsurface coverage of theadsorbedinhibitors isdetermined from polarizationmeasurements, and itwas found thatthe resultsobey theFrumkin adsorption isotherm. Theinhibitorsacted as mixed-typeinhibitors, but the cathode is more polarized.Therelativeinhibitiveefficiencyof thesecompoundshas beenexplained onthe basis of struc­ turedependentelectrondonor properties of the inhibitors and the nature of themetal-inhibitorinteraction atthe surface.Also, some thermodynamicdata for theadsorptionprocess(AGO* andf)arecalculated and discussed.

Introduction

Pickling innitric acid is commonly practised in industry forfinishingmetal surfaces.Theuse of inhibitorsduring the picklingoperation is of very recent origin. Themechanism of theactionofinhibitors for nitric acid has not beenstudied exhaustively.1

Dilute nitric acidis one ofthe best sovlents for copper.

Accordingto Veley,2 copper readilydissolvesinnitrousacid, less readily in a mixture of nitrous and nitric acid and still lessrapidlyinnitricacidalone. The reaction of nitric acid on copper is conditioned by (1) concentration ofthe acid, 2) temperature 3) presenceofnitrousacid, and 4) solubility of thereaction productsin the acid.

Quinine and Strychnine,3 Caffeine,4 n-decylamine,5 2,4- dinitrophenylhydrazine,6 substitutedphenols,7 benzoyl benz­

aldehydehydrazonederivatives8and ethylamine9havebeen usedas effective corrosioninhibitors for copper. Copper is widely used in various industrial operations, therefore the study of the corrosion inhibition ofcopperis a subject of pronounced practicalsignificance.

Thepurposeof the presentcontribution is todeterminethe influence ofsome 2-hydroxyacetophenone aroyl hydrazone derivativestowardsthe corrosionof copper innitric acid, to throw some light on the mechanism of inhibition and to studythe effect of thetemperatureon therateof corrosion.

ExperimentSection

The thermometric reaction vessel and the procedure for determining therate of dissolution of copperin 3 N HNO3 solutionwerethe same as described elsewhere.10Thestudy was carried out with testpieces made of sheets measuring

1 x 10 x 0.2 cm3. Before being used, these were lightly abraded with emery papers of 1/0, 2/0, 3/0 and 4/0 grade thendegreased byacetone. Each experiment was carried out with a new cleanspecimen andwith15 mLof theaggressive

solution.Thevariationofthetemperature of thesystemwas measured to ±0.1oCon a calibratedthermometer. All chem­

icalswereofARquality and were used without furtherpuri­

fication.

The inhibitingefficiencywas calculatedfromthe percent­

agedecreasein RN:

Inhibitionefficiency (%) =

"“縉 "지心

x 100 (1) RNfree

Thereaction numberRN is defined as.11

RN = = AoCmin-1. (2)

where Tm and Tiare the maximum and initialtemperatures respectively,and t is thetime in minutes taken to reach Tm. All experimentswere startedat 30 ± 0.1 oC.

Copper intheformof wire(99.7%)inthe case ofpolariza­

tion measurements,was fixed in glass tubing, such that only a surfacearea of 0.3 cm2was exposed to 100mLof the cor­

rosivemedium. Forpolarization measurements, a saturated calomel electrode and a platinum wire were used as refer­ ence and auxiliary electrodes, respectively. Currents from constantcurrentdevice measured with a multimeter with an accuracy of± 4%.Corrosion potentials wererecorded using a digitalionalizerdevice (Orion model 701A). Thepotential at any given currentunder similarexperimental conditions wasreproducible within 7%.The detailed experimental pro­ cedurehas been given elsewhere.12 Theinhibitiveefficiency wascalculated employing theformula:

where io and iinh. are thecorrosion currentdensities without and with inhibitor, respectively.

Theadditives used as inhibitors wereprepared and crystal­ lized several times according to the general procedure: To ethanolic solution ofthe appropriate aromatic aldehyde-2-

(2)

hydroxy acetophenone, the corresponding acid hydrazides were added. Thereaction mixturewasrefluxed for 2-4hours on a water bath for a time dependingonthe acid hydrazide used. The solution was evaporated till a precipitate is formed. The precipitatewas washedwith hotethanol,diethyl­ ether and dried. The structure of these compounds were identified by elementary, IR, m.p., and NMR analysis. The structureof theinhibitorsarelistedbelow:

1) 2-hydroxyacetophenone-3-aminobenzoyl hydrazone

2) 2-hydroxyacetophenone-3-toloyl hydrazone

OH

13 ?

〈 (j 丿 〉 一

C=N - NH-C

3) 2-hydroxyacetophenone-3-hydroxybenzoyl hydrazone

-1.00 0.00 1.00 2.00

Log i, mA cm'2

Figure 1. Galvanostatic polarization curves of copper in 3 N HNO3 alone and containing different concentrations of compound (1).

4) 2-hydroxyacetophenone-3-chlorobenzoyl hydraozne OH

〈 3 齢q

5) 2-hydroxyacetophenone-3-bromobenzoylhydrazone

6) 2-hydroxyacetophenone-3-nitrobenzoyl hydrazone

Table 1. The effect of compound (1) concentrations on the free corrosion potential (Ecorr), corrosion current density (Crr), Tafel slopes (pa & Bc), inhibition efficiency (Pi) and degree of surface coverage (0) for polarization of copper in 3.0 N HNO3 at 30 oC

Conc.

(M/L) Ecorr.

(mV vs.

SCE)

icorr (mA/cm2)

Pa mV/current

decade

Pc mV/current

decade

%Pi 0

0 50 16.0 60 120 - -

1X10-6 50 9.0 50 110 43 0.43

5x10-6 55 6.2 60 105 61 0.61

1X10-5 55 4.7 60 100 70 0.70

5x10-5 50 3.4 50 95 78 0.78

1X10-4 55 2.3 50 85 86 0.86

5x10-4 60 1.5 60 85 90 0.90

1X10-3 65 0.9 60 95 95 0.95

ResultsandDiscussion

Parization measurements. Corrosionpotentials,corro­ sion currentdensitiesdetermined byextrapolating the catho­

dic and anodic Tafel regions, the intersectis the corrosion currentandcorrosion potential. Figure 1 showsthe galvano- static polarization of copper in 3 N HNO3 solution in the presence and in the absence of various concentrations of compound(1). As can seen, both thecathodicandtheanodic reactions are inhibited and the inhibition increases as the inhibitor concentration increases, but the cathode is more polarized (&> &). Similar results were obtained for other tested compounds. The order of decreasing inhibition effi­

ciencywas foundto be: 1> 2 > 3 > 4 >5> 6 (Table 2). Tafel lines of nearly equal slopes were obtained as can be seen from Table1. This indicates13 that theadsorbed molecules of compound (1) have no effect on the mechanism of either

copper dissolution or hydrogenevolution reaction.

The surface coverage (0) ofthe adsorbedinhibitorswas calculated13 assuming no change in the mechanismof both theanodicandthecathodicreactions using theequation

e =1- (4)

L ^free-^

Figure 2 shows the plot of 0= f (log C) which has the characteristic S-shape. In analysis the isotherms having the S-shape in the 0 -log C system ofco-ordinates, Frumkin’s approach was considered. Frumkin isotherm has the for­

mula:14

BC = (1으-) exp(-0). (5)

B =exp (6)

where C is the concentration of the adsorbed substance in the bulk ofthe solution and B is the modified equilibrium

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0.201_______._______I_______ ,_______ 1_______ ,_______ I

-6.20 -5.20 -4.20 -3.20

Log c, mole L'1

Table 3. Efficiency of corrosion inhibition of 2-hydroxyacetophe- non-aroyl hydrazone derivatives as determined by percentage reduction in reaction number in 3.0 N HNO3

Concentration of the

additive (M/L) % Reduction in R.N.

2 3

Figure 2. Effect of compound (1) concentration on the degree of surface coverage for copper in 3 N HNO3.

constant of the adsorptionprocess. In Eq. (5) f is a constant depending onthe intermolecular interactions inthe adsorp­

tion layerandon the heterogeneityof the metal surface. This parameter caneither be positiveor negative.

Thevalues of B,AGand activationenergy are shown in Table 2.The negative values of AG indicatethespontane­ ousadsorption of inhibitorsoncopper and also, indicate that molecular interactions are notpredominant inthe formation of a protective layer butthe heterogeneity of the surface is thepredominantintheformationof aprotective layer of the inhibitor orits complexeswhich in turn reducethecorrosion rateof copper. One could expectthatthe degree of adsorp­ tion by these inhibitorsoncoppersurfaceis in the order: 1 >

2> 3 > 4 > 5 >6. This is also in agreement with observed orderof corrosioninhibition (Table 1).

Theadsorptionequilibriumconstants(B) for theinhibitors decrease in the order: 1(2.33 x 10-5) > 2(2.23 x 10-5) >

3(1.94x 10-5) > 4(1.70x 10-5) > 5(1.44x 10-5) > 6(1.27x 10-5) (Table 2)indicating increasedadsorption with increas­

ing theelectrondensityon themoleculesofinhibitors.

Thermometricmeasurements. The dissolution of copper in3N HNO3 wasaccompaniedbytemperaturechange.This temperature changewasfollowed in the absence and inthe

Inhibitor B 当損—1 ” f 1—1 % Inhibition Kcal mol Kcal mol

Table 2. Values of thermodynamic parameters during adsorption of 2-hydroxyacetophenone-aroyl hydrazone derivatives (10-5 M) on copper in 3 N HNO3 at 303 K

1 2.33 x 10-5 9.90 12.89 70.0

2 2.23 x 10-5 9.89 11.93 69.0

3 1.94 x 10-5 9.81 11.05 66.0

4 1.70 x 10-5 9.73 10.23 63.0

5 1.44 x 10-5 9.63 9.48 59.0

6 1.27 x 10-5 9.55 8.78 56.0

Free _ — 7.33 —

6 6 5 5 4 - - - - - 0 0 0 0 0 11 11 11 11 11

〉〈〉〈〉〈〉〈〉〈

5 8 3

J 4 4

o 6 5

66 7

847 .4 37 392

.1 4

.3 5 5

.3 7

4 83

Q■°

4 8 z 5

74J 7

829

7 '84 4 5 44 85

6

L 2 3 4 6 8

5 6

.7 1 275

2 354 4 4o5 .9 59 575

o 72 695

presenceof different concentrationsof theadditivesused.

In allcases the dissolution of copper in acid is character­ izedbyinitialslow rise intemperature followedby a sharp rise and finally decrease after attaining a maximum value.

Themaximumtemperature (Tm)measured inthefree acid is 39.8 oC and is attained after 50min., while the Tm in pres­ ence of theadditives used are lowerand are attainedafter a longer time. This indicates thatadditives behave as inhibi­

tors for the dissolution ofcopper in 3 N HNO3, presumably by their adsorptionon thesurface of the metal.

Thepresentthermometric curvesallow distinction between weak and strongadsorption.15 Strong adsorption is notedfor all additives used. The curves of Figure 3 represent this adsorption in thepresence of compound (1).

The fact that the compounds studied bring about a decrease in RN indicates thatthese act as inhibitors. The results recordedin Table 3 reveal that theefficiencyof corro­

sioninhibitionas determined fromthe percentage reduction in RN varies with both concentration and the type ofthe additivesused.

Theinhibitionefficiency oftheadditivesdecreases in the order: 1 > 2 >3> 4 >5>6.

Effect oftemperature. Galvanostaticpolarizationofcop-

° a- ra

o d E

° l

Figure 3. Temperature--time curves obtained in absence and presence of different concentrations of compound (1).

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Figure 4. Log iy. w. 1/T curves for copper dissolution in the presence and absence of 5 x 10-5 M of different inhibitors.

Tafel linesto higher potential regions, 3) thevariationin per­

centagereduction in reaction number with concentrationof the inhibitors, and 4) the decrease in corrosion inhibition with increasingtemperatureindicate that thecorrosioninhi­ bition takes placeby adsorptionofthe inhibitors at theelec­ trode solution interface.18Inhibitionefficiency was shown19 todepend onthenumberofadsorptionactive centers in the molecule andtheir charge density.

Variation in structure of the inhibitors molecules (1-6) takes placethrough thebenzoylsidechain. So, theinhibition efficiencywilldependon thispart of molecule.

Skeletalrepresentationofthe mode of adsorptionofthese compoundsisshown byFigure 5.

Adsorbed moleculesonthe surfaceofthecorrodingmetal interfere with cathodic and/or anodicreactions. Inhibition of

per in3N HNO3 wasstudied inthetemperature range 30-55 oC in absence and in presence of 10-4-10-6 M ofdifferent additives. The rateof corrosionincreases as thetemperature increases i.e. the protection efficiency of the additives decreases with rise in temperature. This behaviour proves that the inhibition of copper dissolution occurs through physicaladsorptionof theadditivesonthe metal surface.

Plots of log icorr. against 1/T for different additives at 5 x 10-5 M as shown in Figure 4 gave straight lines. The valuesof theslopesof thesestraight lines permit the calcula­

tion of the Arrhenius activation energy, E, [logicorr =

.―_ ___ __ - ___ _ _____ 一 . 一

(—EJ2.303RT) + constant] (Table 2). The results reveal that thepresence of inhibitors increasethe activationenergy of copper dissolution reaction. Theactivation energyof cop­

per dissolution in absence of inhibitorswas found tobe 7.33 Kcal mol-1. Fouda et al. 16found thatactivation energy of 4.61 Kcal mol-1 for copper corrosion in 3 N HNO3. Also, Mostafa15 found activation energy of 11.67 Kcalmol-1 for corrosion of copper in 3 N HNO3. This inconsistancy between the literature values of activation energy may be due to: (1) the nature and concentration ofthe electrolytes used and (2) thepurity of copper electrode usedin each case.

The order of decreasinginhibition efficiency of different additives for copper dissolution as gathered from the increase in activationenergy is: 1 > 2 > 3 > 4> 5 >6.

Chemicstructureandcorrosion inhibition of copper.

Inhibition of corrosion of copper in nitric acid bythe investi­

gated2-hyroxyacetophenone-aroyl hydrazone derivatives as determined by galvanostatic polarization and thermometric measurementswasfound to depend ontheconcentration and nature of inhibitor. The observedcorrosion data in the pre­

sence ofinhibitorsnamely: 1) the decrease of corrosionrate with increase in concentrationof the inhibitor,2) the shift in

Compound (3)

Compound (5)

Figure 5. Skeletal representation of the mode of adsorption of these compounds is shown by Figure 5.

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these reactions would obviously depend on the degree of surface coverage ofthe metal with the adsorbate. Competi­ tive adsorption is assumed to occur on the surface ofthe metalbetween theaggressive NO3- ionson one handand the inhibitor molecules on the other. The order ofdecreasing inhibitionefficiency of the tested compounds is: 1 > 2 > 3>

4 >5>6.

This order ofdecreasedinhibitionefficiency of the addi­ tives can be accounted for intermsof the polar effect20 of the m-substituents on the benzoyl ring. Compound (1) is the most efficient inhibitor because of the presence of highly electron releasing m-NH2 (b=-0.16) which enhances the delocalized -electrons on the active centers of the com­ pound. where G is thesubstituentconstnat21 and is a relative measureoftheelectrondensity at the reaction center. More­

over, the nitrogenof NH2 can act as active center and in­ creasesthe active centersintothree. Compound(2)(扁_°电= -0.07) comes next in the sequence ofdecreased inhibition efficiency. This because m-CH3 is lower in electron charge density than m-NH2 and also thiscompoundhas two active centers only. Compound (3) (om-oH=-0.002) follows suit despite the presence of thesame numberofadsorption cen­

ters as compound butOHis lessbasic thanNH2 and CH3, respectively. Compounds (4) (m-Cl, g=0.37), (5) (m-Br,

g=0.39) and (6) (m-NO2, g=0.71), occupytherear and they decreasedcorrosion inhibitionefficiencyof copper parallels an increasing order of electron withdrawing (electrophilic) character. The m-NO2 group with the highest electro­

philic character imparts the lowest inhibition efficiency to inhibitor (6) which comes last among the additives used.

Possible hydrogenation19of theNO2 group inacid medium on the copper surface would also enhance decreased effi­

ciency of inhibitor (6) as the released heat of hydrogenation wouldaid thedesorptionof themolecule.

References

1. Putilova, I. N.; Balezin, S. A.; Barannik, V P. Metallic Corrosion Inhibitors; Pergamon Press Ltd.: Oxford, 1960.

2. Veley, V H. In Comprehensive Treatise on Inorganic and Theoretical Chemistry; Mellor, J. W., Ed.; Longmans, Green and Co. Ltd.: London, 1952.

3. Subramanyan, N. C.; Sheshadria, B. S.; Mayanna, S. M.

Br Corns. J. 1984, 19, 177.

4. Ahmed, M. F.; Mayanna, S. M.; Pushpanaden, F. J. Elec- trochem. Soc. 1977, 124, 1667.

5. Rudre아!, H. B.; Mayanna, S. M. Br Corros. J. 1977, 12, 54.

6. Siddagangappa, S.; Mayanna, S. M.; Pushpanaden, F. Anti Corros. Methods Mater 1976, 23(8), 11.

7. Fouda, A. S.; Mohamed, A. K. Werkst. Korros. 1988, 39, 23.

8. Abdel Maksoud, S. M.; El-Shafie, A. A.; Mostafa, H. A.;

Fouda, A. S. Material and Corrosion 1995, 46, 468.

9. Fouda, A. S.; Mohamed, A. K. J. Electrochem. Soc. Ind.

1990, 39, 246.

10. Aziz, K.; Shams El-Din, A. M. Corros. Sci. 1965, 5, 489.

11. Mylius, F. Z. Metall. 1922, 14, 233.

12. Gatos, H. S. Corrosion NACE 1956, 12, 23t.

13. Abo El-Khair, M. B.; Abdel Hamed, I. A. Corros. Sci.

1976, 16, 169.

14. Frumkin, A. N. J. Phys. Chem. 1925, 116, 46.

15. Saleh, R. M.; Shams El-Din, A. M. Corros. Sci. 1970, 10, 551.

16. Fouda, A. S.; Gomah, S. A.; Moussa, M. N. Qatar Univ.

Sci. J. 1992, 12, 64.

17. Mostafa, A. B. Corros. Prev. Coutrol. 1980, June 70.

18. Rudresh, H. B.; Mayanna, S. M. Surf. Coating Technol.

1977, 6, 139.

19. Fouda, A. S.; Moussa, M. N.; Taha, F. I.; Elneanaa, A. I.

Corros. Sci. 1986, 26, 719.

20. Hammett, L. P. Physical Organic Chemistry; McGraw- Hill Book Co.: N.Y, 1940.

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