Materials 2H03 on-line Laboratory Manual Updated: 24 May 2000 Experiment L Corrosion Objective 1. • To examine and understand the basic electrode processes that control the corrosion rate of a metal. Introduction 2. Corrosion can be defined as the deterioration of a material because of reaction with its environment. Although the cost of such loss is extremely high each year, the same electrochemical processes, if used under controlled conditions, can both refine materials and provide corrosion protection. Corrosion resistance depends on many factors. Thermodynamics indicates the direction of the reaction, electrochemical kinetics control its rate, and microstructural features often determine its location. This introduction describes the simple electrode processes that take place during corrosion of metals in aqueous solutions. 2.a: Single Electrode Processes In general, when one material is placed in contact with another, the atoms will diffuse into the contacted material until the equilibrium solubility is reached. Thus, when a metal plate is put in water, some of the metal atoms will dissolve in the water. These become ionized, i.e., lose one or more electrons, and these remain on the metal. The positive M+ ions, will be attracted back to the negatively charged plate to produce a charged ionic layer that is near the plate. The reaction is M → M+ + e- ....(1) which is called an "anodic" or "oxidation" reaction, since electrons are produced. If nothing else occurred, a negative charge would build up on the plate that would stop the reaction. However, as the concentration of M+ builds up, some of the ions will move back to the metal, i.e., M+ + e- → M ....(2) which is called a "cathodic" or "reduction" reaction, since electrons are consumed. An equilibrium will be reached when the flow of M+ ions from reaction (2) arriving at the metal equals the flow from reaction (1) that leave the metal. We can represent this flow as an electrical current, io, which flows in both directions. Because the ions must overcome a potential barrier in the jumping process (onto or Single Electrode Processes L-1 L-Corrosion off the metal), io is proportional to exp(-Ej/kT). Ej is the jump energy required, k is Boltzmann's constant, and T is degrees Kelvin. At equilibrium, an excess number of electrons has built up on the metal plate, which can be measured with a voltmeter whose other terminal is connected to a reference potential. "Voltage" or "electrostatic potential" is the potential energy per unit positive charge. Thus, the more ions that dissolve; the more excess electrons on the plate; and the more negative its voltage. The voltages produced by different metals are listed as the electrochemical series. All practical corrosion situations are not as ideal as described above. The water can have three types of "impurities" that may replace part of reaction (2). They all produce cathodic reactions. Excess H+, as in an acid, will cause H+ + e - → H ....(3) followed by the formation of hydrogen molecules H + H → H2....(4) Dissolved O2 in acidic solutions will cause O2 + 4H+ +4e- → 2H2O ....(5) and in basic solutions the predominant cathodic reaction will be O2 + 2H2O + 4e- → 4OH- ....(6) These "impurities" will have two effects in our previous description. Reactions 3, 5, and 6 can replace part of reaction 2. Thus, a steady state dissolution (equation 1) will occur as the loss of metal atoms is not canceled by reaction 2. The number of excess electrons on the metal plate will also decrease, which will raise the voltage on the plate to a new volume determined by an equal rate of the anodic reaction 1, with the sum of cathodic reactions 2, 3, 5, and 6. Introduction L-2 L-Corrosion 2.b: Galvanic Cells An open-circuited galvanic cell is produced by putting two different metals, that are not in electrical contact, into water as shown in the sketch. Metal M1 which dissolves more readily than M2, will have more excess electrons and be at a lower voltage. Thus, a positive deflection will be seen on a voltmeter if M1 is connected to the negative terminal and M2 to the positive terminal. M2 is said to be more "noble" than M1, because it does not dissolve as readily. By comparing different pairs of metals, they can be arranged in a sequence of nobility, called the Electromotive Force Series. In the present experiments, NaCl is added to increase the conductivity of the electrolyte solution. In a short-circuited galvanic cell, the metals M1 and M2 are in electrical contact, e.g. by a wire connecting them, as in the sketch of Figure 2. Before the wire is connected (Figure 1), M1 had more excess electrons than M2. Thus, after connection, electrons will flow from M1 to M2. Reducing the negative charge on M1 will make it easier for its anodic reaction, M1 → M1++ e- to proceed. Similarly, the flow of electrons to M2 will reduce the rate of its anodic reaction M2 → M2++ e-. There are some important practical applications of these processes. Cathodic protection of metal M2 has occurred since the rate of its dissolution reaction is reduced. Zinc plates attached to steel will protect the steel. In this case Galvanic Cells L-3 L-Corrosion zinc, or M1 in our example, would function as a sacrificial anode. A similar result occurs if a metal is made cathodic by attaching it to the negative terminal of a battery, which is sometimes done for buried pipelines. In a wet environment, you should not have two metals, which have a large separation in the electromotive force series, in contact with each other, e.g., couplings between pipes in the ground, nails holding the metal roofing, etc. A galvanic cell shunted by a resistor is similar to the short-circuited cell, but the current flow is limited by the value of the resistance. Before contact, there are more excess electrons on M1 than M2. After contact, the electrons will flow through the resistor at a rate inversely proportional to the resistance. This transfer of electrons, enhances the anodic reaction M1 → M1+ + e- on M1, and the cathodic reactions on M2. Its continuation as a current depends on both the continual supply of electrons by the anodic reaction on M1, and removal of electrons by the cathodic reaction at M2. A galvanic cell driven by an external voltage At open circuit, M1 and M2 have their own equilibrium anodic and cathodic currents, io, which are equal and opposite, and proportional to exp(-Ej/kT) as discussed previously. In order to force M1 to have a greater anodic current requires an added voltage η , called the over voltage. The net current will then be η −η i = i 0 exp( ) − exp( ) β β where b depends on kT and the charge on the M1 ion. Thus, for a given net current, i, the actual voltage needed across the cell (using only the first exponential term) is V = V 0 + η = V 0 + βln( i ) i0 where Vo is the open-circuit voltage between M1 and M2. Therefore, a plot of V applied vs ln i should be linear, a so-called Tafel plot. This is called "activation polarization" and is not dependent on time. 2.c: Concentration Polarization This type of polarization usually increases with time, because it depends on diffusion of ions in the liquid. Dissolved ions in the liquid will be located in places Introduction L-4 L-Corrosion that minimize the free energy of the system. This produces an ionic concentration that decreases exponentially with distance from the metal surface, as in the sketch. If the arrival or removal rate of ions from the metal is slow, they have time to redistribute by diffusion in the liquid. (D is commonly 10-5cm2 s-1 in a liquid). If the current is too high, they either pile up near the metal surface for a net anodic current, or are depleted near the surface for a net cathodic current. This causes the current to drop with time if the voltage is held constant, or causes the over potential to increase with time, if the current is held constant. 2.d: Inhibitors and Passivation All the above arguments assumed a relatively easy transfer of ions across the interface between the metal and liquid. If this transfer is made difficult, then the corrosion rate is lower. One way to inhibit this transfer is to add complex molecules that chemisorb on the metal surface. For example, an inhibitor is added to the coolant for cars which have an engine block made from aluminum and radiator or couplings made from other metals. Another way to reduce this transfer of ions is to develop a chemisorbed or oxide layer during the corrosion process. This method, called "Passivation", occurs naturally beyond a critical current density for some metals, if there is a good supply of dissolved oxygen in the water. A typical curve of applied voltage vs. ln i is shown here. Low voltages give the usual straight line, which indicates a logarithmic increase in corrosion rate with applied potential, but the current drops suddenly once a critical current is reached. Current and hence corrosion almost cease for applied voltages within this "passive" region. At much higher potentials oxygen evolution gives a linear rise again in the "transpassive" region. If the very minimal current in the passive region is not maintained, the chemisorbed oxygen or oxide on the metal slowly dissolves. Ni, Ti, Cr, and many stainless steels containing Cr, have very low corrosion rates due to this Passivation process. If the water or atmosphere is sufficiently oxidizing, they will be in the passive region without an applied voltage. Inhibitors and Passivation L-5 L-Corrosion 2.e: Non-uniform "pitting" and "crevice" corrosion If there are non-uniformities in the chemical composition of either the material or the environment at its surface, then both local anodes and cathodes can exist on the same piece of metal. The region that is locally anodic will corrode forming a pit. The inhomogeneities are frequently caused by depletion of one of the reactants. For instance, the oxygen supply under the centre of a water droplet, or at the bottom of the crevices is quickly used up. This slows the local cathodic reaction, which makes it locally anodic with respect to other areas. Reference: Jastrzebski, "The Nature and Properties of Engineering Materials", J. Wiley, 1987. Procedure for the First Afternoon 3. Read parts 1-5, and 7 of the introduction before the first lab period. If uncertain about anything ask the demonstrator before you do the experiments. 3.a: Galvanic couples Sheets of Cu, Zn, Sn and mild steel are provided for electrodes. Clean them with abrasive paper. Place each possible combination (6 pairs) of the four electrodes into a 3% NaCl solution that fills one third of a 600 ml beaker. Measure the peak voltage generated and the sign of each electrode. If the voltage is still increasing after 2 minutes, take the value at 2 minutes. (A voltmeter draws very little current because it has an extremely high resistance). Knowing the polarity, deduce the direction of the electron flow, and decide which metal is the anode and cathode in each pair. Which metal in each pair is corroding? Using your results, list these four metals in a galvanic series from least noble to most noble. Note: the "electric current" is defined as the flow of positive charge from a positive to negative voltage. The meter reads this electric current. Electrons will be flowing in the opposite direction, from the negative terminal to the positive terminal. For a positive reading, Procedure for the First Afternoon L-6 L-Corrosion the positive terminal on the voltmeter or ammeter is connected to the positive electrode (i.e., the cathode). 3.b: Concentration polarization Using the Cu and Zn electrodes, set up the circuit shown. Measure the open-circuit voltage (i.e., switch not closed). Now set the resistance to 1000 ohms, close the switch and record the current and voltage at 15 second intervals for 5 minutes. Remeasure the open circuit voltage. If this does not agree with earlier readings, stir the electrolyte with the electrodes and try again. Repeat this for resistance of 500 and 200 ohms, including the remeasurement of open circuit voltage. Add a few ml of peroxide (H2O2), which forms H2O+ ½ O2 when put in water, and repeat the experiment using 200 ohms resistance. Clean and dry all electrodes. Throw out the electrolyte. In your writeup, compare the results by plotting current and voltage vs. time. Explain the results in terms of the flow of electrons, and of specific ions at the cathode surface. Also explain why stirring the electrolyte restores the voltage. 3.c: Anodes and cathodes At the beginning of the session, prepare the mixed indicator gel containing 7.5 g NaCl dissolved in 250 ml distilled water. Boil it and add 5 g agar. Boil and stir until agar dissolves. Add 5 ml potassium ferricyanide and 5 ml of 1% phenolphthalein solution. Pour some of the fluid gel into a petri dish and drop into it, without disturbance, Samples • A short piece of the steel wire. Anodes and cathodes L-7 L-Corrosion • A similar piece that has been bent back and forth many times to form a sharp U shape, and • A steel/zinc combination • A steel/tin combination. Clean an area 75 mm square in the centre of a piece of steel sheet with abrasive paper. Pour into the middle of this a small pool of the indicator gel and immediately press the convex face of the watch onto the steel surface to make contact.. Place a few drops of indicator on the cleaned surface of another steel sheet. Observe what you see during the afternoon, and save the samples for another look at the second session. Note: In the presence of Fe++, the ferricyanide will turn blue. The phenolphthalein turns pink with excess OH-. With this knowledge, plus the observations from part (b), and considering the crevice between the glass and steel, explain the pink, white, and blue colour changes observed. When your examination is complete, remember to remove the specimens, wash and dry them, put the gel in the container provided for disposal, wash the Petri dish ! In the next experiments, the change in potential (voltage), of the steel is measured by comparison with a reference potential, that is produced by a Cu plate immersed in a saturated Cu2SO4 solution, i.e., a simple reference electrode. Procedure for the First Afternoon L-8 L-Corrosion 3.d: Sacrificial Anode 1. Measure the weight of the ZINC electrode. 2. Place the steel electrode into a 3% NaCl solution and set up the Cu/Cu2SO4 reference cell and circuit as shown by solid lines in the accompanying figure. Connect the two beakers with the salt bridge. Measure current and voltage. Record polarity. 3. Connect an immersed piece of Cu wire to "above" the ammeter, as shown dotted in the sketch. Remeasure current, voltage and record polarity. 4. Connect an immersed piece of Zn sheet to "above" the ammeter, as shown dotted in the sketch. Remeasure current, voltage and record polarity. 5. Remove the Zn sheet. Measure the current and voltage. Add a commercial inhibitor and remeasure the current and voltage. 6. Remove all the steel and Cu electrodes. Wash them and measure the approximate total immersed surface area of the steel and zinc sheet. 7. Re-Measure the weight of the ZINC electrode. In your writeup, explain the voltage, current, and polarity changes in parts (iii) and (iv). Which metal is corroding in part (iii) and in part (iv)? If the steel sample represents a ship hull to be protected, what would be the weight of zinc anode per m2 of structure consumed in a year to protect it? According to Faraday's Law: Sacrificial Anode L-9 L-Corrosion (weightofzincdissolved ) it = (GAW Zn ) nF where GAW = gramatomic weight, i = current in amps, t = seconds, n = charge on Zn ion, and F = Faraday's constant =96,500 coulomb per mole. If the steel is protected now by a paint layer, whose pores cover 0.1% of the area, what would be the new consumption of zinc? Procedure for the Second Afternoon 4. 4.a: Polarization Curve The Measurement of the Polarization Curve of 430 Stainless Steel with a Potentiostat (HA-151) 1. Read part 6 of the introduction and the description of the potentiostat used in this experiment (available in the lab). 2. Before connecting or disconnecting the power cable, be sure to turn off the power switch of the potentiostat. 3. There are two pieces of 430 stainless steel to be used as electrodes. Set them up with the straight piece connected to the WE1 abd WE2 of the TO-CELL-OUT cable of the potentiostat (one connection is used to measure voltage while the other is used to measure current), and the curved piece connected to the CE terminal. Procedure for the Second Afternoon L-10 L-Corrosion 4. The reference electrode to be used is Cu/Cu2SO4. Connect the piece of copper to the RE terminal of the TO-CELL-OUT cable of the potentiostat. 5. Pour the 6% H2SO4 solution into the beaker with the two pieces of stainless steel, and pour the Cu2SO4 solution into the beaker with the piece of copper. Connect the two beakers with a salt bridge. 6. Before turning on the potentiostat, make sure the FUNCTION selector is set to ZERO ADJ. Turn on the potentiostat. 7. Set the P-STAT/G-STAT selector to P-STAT (potentiostat), and set the EXT.SET selector to the OFF position. The potentiostat is now ready to be used. The starting value of the potential will be the equilibrium potential, defined as the potential of the working electrode with respect to that of the reference electrode at zero current. 8. To measure the equilibrium potential, the FUNCTION selector should be set to REST POT, and the POTENTIAL/CURRENT selector should be set at 2V. The green voltage light should be on. 9. The polarity can be set at either + or - using the POLARITY selector. A positive potential reading with the POLARITY set to + , means that the potential of the working electrode is higher than that of the reference electrode. The potential value is displayed on the digital meter on the front panel of the potentiostat. 10. Once the equilibrium potential has been measured, set the FUNCTION selector to OPERATION. You can now maintain the potential at any value you choose. 11. Increase the potential by 50 mV. Take readings of both potential and current from the digital meter. To obtain the current values, switch the POTENTIAL/CURRENT selector to CURRENT with a suitable current range. If the current reading is unstable, take the current reading after 30 seconds. 12. Repeat step (k) until you have obtained enough data to plot the Passivation curve. 13. Dissolve 10 g of NaCl in the H2SO4 solution. Repeat steps (h) through (l). The presence of Cl- is expected to diminish the passivity range and increase the passive current density. Once you have completed the above steps, you must close down the system and clean the equipment: Polarization Curve L-11 L-Corrosion 14. Set the FUNCTION selector to ZERO ADJ. Turn off the power to the potentiostat. 15. Return the Cu2SO4 solution to the bottle. Remove the salt bridge, and store it in a beaker filled with distilled water. Clean the metal sheets and the beakers used. 16. Measure the approximate immersed surface area of the straight piece of stainless steel used as the working electrode (don’t forget to account for both sides of the steel). 5. Writeup Plot the data obtained for both cases (i.e., with and without NaCl) as E vs log i , where E and i are potential and current density (A/cm2) respectively. Answer the following questions for each curve: 1. What is the potential range corresponding to passivity? 2. What is the minimum potential necessary to preserve passivity? 3. Discuss the differences observed in the two curves. Writeup L-12
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