Study of the Protection of Mild Steel Corrosion with Piperidin -4-One and Its Semicarbazones

DOI : 10.17577/IJERTV2IS60845

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Study of the Protection of Mild Steel Corrosion with Piperidin -4-One and Its Semicarbazones

Dr. L. Ravikumar *, Dr .G. Rathika*, R. Punitha**

*Associate Professor, CBM College of arts and science

* Professor, P. S. G College of arts and science

** Assistance Professor Sree Sakthi Engineering College

Abstract

Three new Schiff bases viz r-2 c-6 Diphenyl-t-3- methyl piperidine-4-one [S1],r-2,c-6-diphenyl-t-3- methyl-N-methyl piperidine-4-one semicarbazone [S2] and r-2 c-6-Diphenyl-t-3-methyl piperidine-4- one semicarbazone [S3] have been investigated as corrosion inhibitors for mild steel in 1M H2SO4 using weight loss, Tafel polarization, electron chemical impedance spectroscopy (EIS) and scanning electron microscopy (SEM). The three Schiff bases function as good inhibitors reaching inhibition efficiencies of

~ 93-94% at 7mM concentration. The fraction

<theta> of the metal surface covered by the inhibitor is found to increase with inhibitor concentration of the three Schiff bases, the S2 shown better efficiency than the other two Schiff bases. The adsorption of the inhibitor follows Longmuir isotherm. Thermodynamic calculations indicate the adsorption to be physical in nature.

1. Introduction

The inhibiting influence of piperidine and its semicarbazones has been investigated this influence is attributed to the adsorption of these compounds through-NH and C=0 group of piperidone to the metal surface. In the case of piperidin-4-one semicarbazones the inhibition efficiency was found to increase. This shows the involvement of NH and

CO groups in

Semicarbazone moiety in addition to Nitrogen of piperidone ring [1]. The previous considerations led us to synthesizing the inhibitor molecules with structures depicted in Fig(1), namely. r-2, C-6 Diphenyl-t-3-methyl piperidine-4-one[S1],r-2,C-6- Diphenyl-t-3-methyl-N-methylpiperidine-4-one semicarbazones[S2] to compare the reactivity of three inhibitors, its order of reactivity is S1<S3<S2, The S3 compared to that of S1 has better inhibitor efficiency, due to the presence of C0-and NH group which is present in semicarbazone, where as in the case of inhibitor S2 in addition to CO and -NH group an hydrogen attached to the ring nitrogen of S3 has been replaced by CH3 group enhances the inhibition efficiency. In the present paper the efficiency of S1, S2 and S3 as inhibitors for the corrosion of mild steel in 1M H2SO4 discussed on the basis of weight loss, Tafel polarization, AC Impedance spectroscopy and scanning electron microscopy (SEM) data.

O

H3C

Ph N Ph H

(S1)

H3C

O

N – NH – C – NH 2

prepared by just heating the mixture of dry ammonium acetate in glacial acetic acid, benzaldehyde and butanone and allowed to stand overnight then, conc. HCl was added and then the precipitate washed with ethanol ether. The inhibitor

Ph N Ph CH3

(S2)

O

S2 and S3 were prepared from S1. The r-2, c-6 diphenyl-t-3-methyl piperidine-4-one was dissolved in acetone, then potassium carbonate and dimethyl sulphate salts were added. The mixture refluxed over a water bath, dilution with water followed by treatment with ammonia gave S2. r-2, c-6-diphenyl,-t- 3- methyl N-methyl piperidine-4-one and it is added with semicarbazide hydrochloride and sodium acetate

H3C

N – NH – C – NH 2

dissolved in ethanol. This mixture shaken well for about 15 min to obtained inhibitor S2. The inhibitor S3 was prepared by adding semicarbazide hydrochloride and sodium acetate in hot ethanol and

Ph N Ph H

(S3)

Figure 1. Structure of the inhibitors S1, S2 and S3

2. Experimental

2.1. Electrodes

Working electrodes were prepared using mild steel specimens of size (5cm x 2.5 cm x 0.1cm). The plates were washed, dried and polished successively using emery sheets of 1/0, 2/0, 3/0 and 4/0 grades to remove adhering impurities finally degreased with acetone and dried using a drier. For electrochemical study the cylinder of the mild steel having diameter 5mM were embedded in a Teflon holder with an exposed area of 1sq cm was used for the present study. The mild steel electrode, counter electrode and saturated calomel electrodes were used. To obtain the stabilized open circuit potential (OCP), the samples were immersed 20-30 min in the solution before EIS and Tafel polarization

measurements.

    1. Inhibitors

      The inhibitors with structures shown in Fig.1 were synthesized according to the procedure that of Balasubramanian and Padma [2]. Briefly S1,

      mixed with inhibitor S1. The solution was shaken well for about 15 min. The product formed was filtered and washed with water.

      All chemicals were of analytical reagent grade and were used without future purification, and inhibitor solutions were prepared in1M H2SO4 to which 5% ethanol was added for solubility reasons.

    2. Equipment

Mild steel specimens of size 5cm x 2.5cm x 0.1cm, 200 ml glass beaker and glass hooks were used for weight loss method, electrochemical impedance. Spectroscopy (EIS) and Tafel Polarization were calculated in an electrochemical measurement unit (Model 1280 B solar ton, Ok). The EIS measurements were made at corrosion potentials over a frequency range of 10 KHz to 0.01 KHz with a signal amplified of 10mv. The Tafel polarization measurements were made after EIS studies for a potential rage of -200 mv to +200 mv with respect to open circuit potential (OCP), at a scan rate of 1mv/ Sec.

The Icorr, Ecorr, Rt and Cdl values were obtained from the data using the corresponding Corrview and Zview softwares. Surface of mild steel specimens were examined using scanning electron microscope (SEM) in order to understand the surface morphology of the mild steel. The surface morphology was taken using JEOL Scanning electron microscope.

3. Results and Discussion

3.1 Weight Loss Studies

The weight loss method was carried out using various concentrations (i.e. 0.5mM -7mM) of

the inhibitors namely S ,S and S in IM H SO . In

The effect of concentration of inhibitor on weight loss measurements were obtained by plotting weight loss Vs inhibitor concentration as shown in Fig (2). This reveals that the metal loss progressively decreased with the increasing inhibitor concentrations. The corrosion rate in IM H2SO4 for various concentrations of the inhibitors (S1, S2, and S3) was determined by using the formula.

1 2 3 2 4

this study the parameters like corrosion rate (mpy), surface coverage (), inhibition efficiency and adsorption isotherm were calculated. The above results were given in Table (1).

Table 1. Inhibition efficiencies of various concentrations of inhibitor (S2) for the corrosion of mild steel in 1M H2SO4 obtained by weight loss measurements at room temperature

Corrosion Rate = 534 x Weight Loss in mgm (mpy) Density x Area x time in hours

Where

W – Weight loss in mg D – Density in g/cc

A – Area of Exposure in cm2 and

T – Time in hours

The corrosion rate expressed in mpy decreased with increasing inhibitor concentration as evident from table (1) and shown in Fig (3). The surface coverage for different inhibitor concentrations were calculated by using the formula

= W b-W i

W b

from this a graph was drawn between C/ Vs C as shown in Fig(4). From this fig a straight line confirming that the pipleridine-4-one semicnbazones obeyed Langmuir adsorption isotherm.

Name of the inhibit or

Inhi bitor Conc.(mM)

Weight loss (gms)

Inhibi tion efficie ncy (%)

Corrosion rate (mpy)

Degree of Covera ge ()

S2

Blank

0.3672

8379.69

0.5

0.0547

85.1

1248.28

0.8510

1

0.0487

86.74

1111.36

0.8674

1.5

0.0457

87.55

1042.89

0.8755

2

0.0397

89.19

905.97

0.8919

2.5

0.0348

90.52

794.15

0.9052

3

0.0318

91.34

725.69

0.9134

5

0.0262

92.86

597.89

0.9286

7

0.0203

94.47

462.26

0.9447

Name of the inhibit or

Inhi bitor Conc. (mM)

Weight loss (gms)

Inhibi tion efficie ncy (%)

Corrosion rate (mpy)

Degree of Covera ge ()

S2

Blank

0.3672

8379.69

0.5

0.0547

85.1

1248.28

0.8510

1

0.0487

86.74

1111.36

0.8674

1.5

0.0457

87.55

1042.89

0.8755

2

0.0397

89.19

905.97

0.8919

2.5

0.0348

90.52

794.15

0.9052

3

0.0318

91.34

725.69

0.9134

5

0.0262

92.86

597.89

0.9286

7

0.0203

94.47

462.26

0.9447

0.14

0.12

0.1

S1

SS21 S3

The effect of concentration of inhibitor on inhibition efficiency was determined by using the following relationship.

W0- Wi

I.E ( %) = x100 W0

Where W o is the weight loss without

Weight Loss (gms)

0.08

0.08

0.06

0.04

0.02

0

0 1 2 3 4 5 6 7 8

Concentration (mM)

inhibitor and W i is the weight loss with inhibitor. From this the inhibition efficiency was found to increase with increasing inhibitor concentration.

Figure 2. The effect of concentration of inhibitor on weight loss in IM H2SO4

The values of activation energy (Ea) were calculated from the plot of log (corrosion rate) Vs 1000/T. The

0.14 free energy of adsorption (Go ) at various

0.12

S1

S1

S2

S2

S3

S3

0.1

0.08

0.06

0.06

Corrosion Rate (mpy)

0.04

0.02

0

0 1 2 3 4 5 6 7 8

Concentration (mM)

Figure 3. The effect of concentration of inhibitor

ads

temperatures was calculated using the following equation.

ads

ads

Go = – RT ln (55.5K)

Where K is the equilibrium constant and it is given by

K = /C (1-) (from, Langmuir equation)

= Degree of coverage on the metal surface. C =Concentration of inhibitor in mM.

R =Gas constant and T =Temperature

ads

ads

G

G

The decrease in IE with temperature indicates the fact that the inhibitor film formed on the metal surface is less protective in nature at higher temperature [3] . The values of Ea and Go are given in Table (2). The less negative values of

on corrosion rate in IM H2SO4

o

ads

phy

with increase in temperature indicate the adsorption of Schiff bases of piperidin-4-one

9

8

7

6

5

C/4

3

2

sical

and its semicarbazones on the metal surface [4]. The values of Ea in the inhibited acid solution are appreciable for greater than those obtained in the uninhibited acid solutions. This suggests that the presence of reactive centers on the inhibitors, block the active sites for corrosion resulting in an increase in Ea [5].

S1 Table.2 Activation energies (Ea) and free energies of adsorption (G° ads ) for the corrosion of mild

S2 steel in 1M H2SO4 at selected concentration of the

S3 inhibitors

Name of the Inhibitor

Ea 40°C –

60°C KJ

G°ads at various temperature KJ

40°C

50°C

60°C

Blank

17.998

S1

24.125

-4.28

-2.05

-1.08

S2

32.162

-7.73

-2.75

-1.3

S3

23.359

-6.01

-2.43

-1.25

Name of the Inhibitor

Ea 40°C –

60°C KJ

G°ads at various temperature KJ

40°C

50°C

60°C

Blank

17.998

S1

24.125

-4.28

-2.05

-1.08

S2

32.162

-7.73

-2.75

-1.3

S3

23.359

-6.01

-2.43

-1.25

0 2 3 4 5 6 7 8

Concentration (mM)

Figure 4. The effect of concentration of inhibitor on C/

3.2. Adsorption Isotherm and Thermodynamic Calculations.

In IM H2SO4 the dissolution of metal increases with rise in temperature both in presence and absence of inhibitor and efficiency of the inhibitor decrease with increase in temperature indicating weak adsorption this is shown in Table(2).

    1. Electrochemical Studies

      3.3.1 A.C. Impedance Method

      Fig (5) shows a typical set of complex plane plots of mild steel in 1M H2SO4 in the absence and presence of various concentrations of the shiff bases to the acid media. Increasing the concentration of the inhibitor caused the values of charge transfer resistance to shift to elevated amounts this can be calculated using the formula.

      I.E (%) = R t(blank) R t (inh)

      R t(blank)

      Where R t(inh) and R t(blank) is the charge transfer resistance in the presence and absence of inhibitor steel in 1M H2SO4 .Of the three inhibitors the S2 show better efficiency than the other two inhibitors. This can be related to the structure of the molecule and its more adsorption centers on metal surface.

      Figure 5. Impedance curve for the Inhibitor S1and S2

      From the table(3) the decrease in the double layer capacitance (Cdl) values may be attributed to decrease in local dielectric constant or an increase in the thickness of the electrical double layer(6). The double layer capacitance (Cdl) decreases with increasing inhibitor concentration. The decreases in Cdl values in presence of inhibitors indicate the fact that theseadditives inhibit corrosion by adsorption on the metal surface (7).

      Table.3. A.C- Impedance parameters for mild steel for selected concentrations

      of the inhibitors S1, S2 and S3 in 1M H2SO4

      Name of the Inhibitor

      Inhibitor concentration (mM)

      Rt (ohm cm2 )

      Cdl (Fcm-

      2)

      Inhibition efficiency (%)

      S1

      Blank

      1.037

      1.671

      1.0

      2.305

      2.348

      5.0

      2.855

      1.550

      63.68

      7.0

      3.464

      1.441

      70.06

      S2

      1.0

      2.812

      1.878

      63.12

      7.0

      4.669

      1.667

      77.79

      S3

      5.0

      2.519

      1.942

      70.53

      7.0

      4.172

      1.765

      75.14

      3.3.2. Tafel polarization

      Fig (8) shows a typical record of Tafel polarization measurement for mild steel in 1M H2SO4 in the absence and presence of the inhibitor. The inhibition efficiency is calculated from the value of I corr by using the formula

      I.E (%)= I corr (blank) – I corr (inh)

      I corr (blank)

      where I corr(blank) and Icorr (inh) is the corrosion current in the presence and absence of the inhibitor. The corrosion current density (icorr) of blank mild steel electrode in this condition was 261.43 A cm-2 . It is clear that corrosion current density decreases with increasing the concentration of the inhibitors.

      Addition of the inhibitor to acid media affects both the cathodic and anodic parts of the curves therefore these compounds behave as mixed inhibitors [8].

      Table.4. Corrosion parameters for the mild steel with selected concentrations

      of the inhibitors in 1M H2SO4 by potentiodynamic polarization method

      Name of the Inhibi tor

      Inhibitor concentr ation (mM)

      Tafel Slopes

      Ecorr (mu)

      Icorr (A/ cm2)

      Inhib ition effici ency (%)

      ba

      bc

      S1

      Blank

      1268

      1391

      -467.77

      261.4

      3

      1.0

      1011

      1123

      -457.66

      99.26

      62.03

      5.0

      1016

      1126

      -462.29

      90.92

      65.47

      7.0

      1012

      1120

      -455.91

      86.47

      66.92

      S2

      1.0

      1007

      1119

      -469.69

      78.47

      69.98

      5.0

      1003

      1112

      -463.99

      49.54

      81.05

      7 .0

      1005

      1115

      -469.39

      37.34

      89.75

      S3

      5.0

      1003

      1107

      -461.23

      76.79

      70.62

      7.0

      1007

      1109

      -467.89

      56.23

      78.49

    2. Scanning Electron Microscopic Study [SEM]

Figure 8. Polarization curves for inhibitor S1 and S2

Table (4) lists the polarization parameters for corrosion of mild steel in the presence of different concentrations of the investigated inhibitors. From this it is seen that the corrosion current density decreases when the concentration of the inhibitor increases, so the studied inhibitor cause a decrease in corrosion rate of steel in acid media by influencing both the anodic and cathodic reactions.

Surface of polished mild steel specimen immersed in 1M H2SO4 in the absence and presence of inhibitors such as S1,S2 and S3 were examined using scanning electron microscope (SEM) it was shown in Fig(9). From this Fig (9a) in the case of blank corroded metal surface with etched grain boundaries the corrosion products are clearly seen. But in the presence of inhibitors, there is a formation of adsorption layer of inhibitors on the metal surface without any corrosion products, as seen in Fig (9b) only some original surface defects of the specimens are seen. Hence all the inhibitors having good inhibition efficiency is revealed.

4. Conclusion

All these studied inhibitors are good inhibitors for mild steel corrosion in sulphuric acid solution, generating inhibition efficiencies in the order of 94% at a concentration of 7mM. For low concentrations S1 and S3 are indistinguishable in performance, as the concentration increases S2 shows an increasing inhibitive advantage over S1 and S3.

The adsorption of the compounds on the metal surface is found to obey Longmuir adsorption isotherm.

The activation energy is higher for the inhibited acids than for the uninhibited acids showing the temperature dependence of inhibition efficiency and also the less negative Goads values indicate spontaneous adsorption of the inhibitors on the metal surface.

Electrochemical impedance spectroscopy experiments have shown that an increase in inhibitor concentration cause an increase in polarization resistance R t and a decrease in Cdl values, owing to the increased thickness of the adsorbed layer.

Tafel slopes obtained from potentiodynamic polarization curves indicates that the compounds behave as a mixed type indicator.

Scanning electron Microscope (SEM) study reveals the formation of a smooth, dense protective layer in presence of an effective inhibitor.

References

  1. S.Muralidharan, R.Chandrasekar and S.V.K. Iyer, Pro. Indian. Aca,Chemical Science, 112,No.(2),2000,pp.27- 1336.

  2. M.Balasubramanian and N. Padma, Tetrahedron,19,1963,2135.

  3. M.A.Guraishi,M.Wajiid Khan, M.Ajmal,S.Muralidharan and S.V.K.Iyer, Anti Corrosion Methods and Material,43,1996,5.

  4. M.S. Abdel-AAI and M.S. Morad, British Corrosion Journal,36,2001,253.

  5. I.M.Putilova, S.A. Balezin and U.P. Baranik, Metallic Corrosion Inhibitors, Pergmon Press , New York, 1960,p.31.

  6. M.G. Hosseini, M. Ehteshamzadesh and T.Shahrabi, Electrochimica Acta, 52,2007,3680.

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