logging in or signing up UN1001 Galvanic Corrosion Cubemiddle Download Post to : URL : Related Presentations : Share Add to Flag Embed Email Send to Blogs and Networks Add to Favorites Add to Channel Uploaded from authorPOINTLite Insert YouTube videos in PowerPont slides with aS Desktop Copy embed code: (To copy code, click on the text box) Embed: URL: Thumbnail: WordPress Embed Customize Embed The presentation is successfully added In Your Favorites. Views: 3405 Category: Entertainment License: All Rights Reserved Like it (3) Dislike it (1) Added: January 02, 2008 This Presentation is Public Favorites: 1 Presentation Description No description available. Comments Posting comment... By: durvesh16 (4 month(s) ago) wow great ppt Saving..... Post Reply Close Saving..... Edit Comment Close By: anilshegaon (12 month(s) ago) Very Well described and nicely put all the data in the presentation. Please send the said presentation to anilshegaon@yahoo.co.in With Warm Reagrds Anil Saving..... Post Reply Close Saving..... Edit Comment Close By: sudhirmaingi1974 (38 month(s) ago) Hello friend.. I m SUDHIR KUMAR working as lecturer in chemistry in kendriya vidyalaya vv nagar anand . I like very much your work on corrosion. Kindly send it to me at sudhir_maingi@rediffmail.com. Saving..... Post Reply Close Saving..... Edit Comment Close Premium member Presentation Transcript UN1001: REACTOR CHEMISTRY AND CORROSION Section 4: Galvanic Corrosion: UN1001: REACTOR CHEMISTRY AND CORROSION Section 4: Galvanic Corrosion By D.H. Lister & W.G. Cook Department of Chemical Engineering University of New BrunswickThe Eight Forms of Corrosion: The Eight Forms of Corrosion Uniform attack (general corrosion); Galvanic corrosion; Crevice corrosion; Pitting; Intergraular attack (“IGA”); Selective leaching; Flow-Accelerated Corrosion; Stress corrosion cracking (“SCC”) Slide3: Remember - electrochemistry basics in aqueous solution: metal dissolution is ANODIC: M Mn+ + n e- (e.g. Fe Fe 2+ + 2 e-) Slide4: and there are several possible CATHODIC reactions: hydrogen evolution (acids) 2 H+ + 2 e- H2 oxygen reduction (acids) O2 + 4H+ + 4 e- 2 H2O oxygen reduction (neutral or base) O2 + 2 H2O + 4 e- 4 OH- metal ion reduction M3+ + e- M2+ metal deposition M+ + e- M Note: More than one oxidation and more than one reduction reaction can occur during corrosion.Slide5: MULTIPLE CATHODIC REACTIONS ARE IMPORTANT. Thus, metals tend to dissolve more readily in aerated acids than in pure, de-aerated acid: In aerated acids, oxygen reduction AND hydrogen evolution can occur simultaneously: 2 H+ + 2 e- H2 O2 + 4H+ + 4 e- 2 H2O Also, an oxidizer, such as ferric ion, as an impurity in commercial acids makes them much more corrosive than pure acids because of the extra cathodic reaction that may occur: Fe3+ + e- Fe2+Slide6: Note: corrosion in sea water (or fresh water) is usually governed by oxygen reduction. If water is de-aerated, it becomes much less corrosive because the main reaction: O2 + 2 H2O + 4 e- 4 OH- can no longer occur. The cathodic reaction in absence of oxygen is hydrogen evolution: 2 H+ + 2 e- H2Slide7: REMEMBER: the metal dissolution reaction (corrosion) must always be balanced by one or more reduction reactions: For example, in neutral or alkaline water: 2 Fe 2 Fe2+ + 4 e- + O2 + 2 H2O + 4 e- 4 OH- 2 Fe + O2 + 2 H2O 2 Fe2+ + 4 OH- Fe2+ hydrolyses and precipitates, and is then oxidised to rust: 2 Fe(OH)2 ↓ + 1/2 O2 + H2O → 2 Fe(OH)3 Slide8: What about iron in a copper solution? Fe Fe2+ + 2 e- Cu2+ + 2 e- Cu Fe + Cu2+ Fe2+ + Cu (the old “nail in copper sulphate” trick!) clearly, the iron wants to be in solution more than the copper. the copper is more NOBLE than the iron; the iron is more ACTIVE than the copper. GALVANIC SERIES: A metal in contact with a solution establishes a POTENTIAL with respect to the solution How would we measure the potential difference Em - Es? GALVANIC SERIESSlide10: Em - Es cannot be measured, we can only measure the difference between it and Em - Es for another metal: (Em1 - Es) - (Em2 - Es) = Em1 - Em2 Slide11: CHANGES in potential of one electrode can be measured if the other electrode does not change, i.e. if it is a reference electrode. There are several reference electrodes which are constant so long as no current is drawn from them; Potentials relative to a reference electrode are therefore measured with meters (e.g. milli-voltmeters) of high impedance.Slide13: A metal in contact with a solution of its own ions at unit activity (thermodynamic concentration) establishes fixed potential differences with respect to every other metal in the same condition OF EQUILIBRIUM (potentials are reversible); THEREFORE, we can set up a series of standard electrode potentials with respect to some reference electrode; The standard hydrogen electrode (SHE) is chosen to have a potential of zero at 25C.Slide15: This has the accepted sign convention; however, some workers use opposite sign convention. These potentials are listed in accordance with the Stockholm Convention. See J. O’M. Bockris and A. K. N. Reddy, Modern Electrochemistry, Plenum Press, New York, 2002 COMMON REFERENCE ELECTRODES: COMMON REFERENCE ELECTRODES Ag(s)/AgCl(s) in 0.1 M KCl: + 0.288 V (SHE) in sat. KCl: +0.192 V (SHE) Cu(s)/Cu SO4 (saturated): + 0.316 V (SHE) Hg(s)/ Hg2Cl2(s) in 0.1 M KCl: + 0.334 V (SHE) in sat. KCl: +0.242 V (SHE) Slide17: By coupling two reversible electrodes together, we get a fixed potential difference: e.g. Ag / Ag+ - Cu2+ / Cu = 0.799 V - 0.337 V = 0.462 V (Discuss the possibility of making a reversible electrode out of an alloy such as brass.) Slide18: Note: If we drew current from two such electrodes (reversible Ag, Cu) THEY WOULD NO LONGER BE AT EQUILIBRIUM. THE REVERSIBILITY WOULD BE DESTROYED. silver would be deposited more than silver ions would be formed; copper ions would be formed more than copper would be deposited;Slide19: (remember, equilibrium or reversibility at an electrode means the rate of the forward reaction equals the rate of the back reaction). Another note: Corroding metals are not at equilibrium NOR are they usually in contact with unit activity of their own ions. THEREFORE the EMF series is an ideal system, which may be used as an indicator for practical situations. Slide20: IN GENERAL, as a rough guide: any metal in the EMF series will displace from solution any metal above it e.g. Fe displaces Cu from CuSO4 solution Zn displaces H2 from acid solution. BUT passivation of some metals alters its behavior; Slide21: Passivation is the formation of a very protective oxide layer that makes the metal more noble than it otherwise would be. e.g. Cr is a fairly reactive element, but Cr metal is usually passivated and cathodic to most common metals (hence chrome plating).Slide22: Galvanic corrosion MAY arise when dissimilar metals are in contact in aqueous solution. The potential difference between them will initiate attack, the corrosion rate depends on the surface reactions of (usually) both metals (i.e. we usually consider galvanic COUPLES of just two metals). Slide23: Galvanic potentials are made use of in batteries, e.g. the Daniel cell. In the Daniel cell, the zinc electrode is 1.1V negative with respect to the copper electrode. Which is the anode, the cathode? Which way does the electrical current flow?Slide24: The sign of the voltage on the Daniel cell indicates that, upon placing a load on the cell, a spontaneous de-electronation will occur on the zinc electrode; and electronation, on the copper electrode. Slide25: A Dry Cell: Dry cells are electrochemical energy storers in which the electrolyte is immobilized in the form of a paste. A typical dry cell is the Leclanche cell. A schematic diagram of this cell is shown below. The reactions occurring in the cell during discharge are: at the anode: Zn Zn2+ + 2 e- at the cathode: 2 MnO2 + 2 H3O+ + 2 e- Mn2O3 + 3 H2O Or 2 MnO2 + H2O + 2 e- Mn2O3 + 2 OH- Slide27: Since hydroxide ions are produced during working (because H3O+ is consumed), the following irreversible side reactions occur: OH- + NH4+ H2O + NH3 Zn2+ + 2 NH3 + 2 Cl- Zn(NH3)2Cl2 Zn2+ + 2 OH- ZnO + H2O ZnO + Mn2O3 Mn2O3 ZnO Owing to the above reactions, the cell is only partially rechargeable and this to such a small extent that it is never done in practice. Slide28: NOTE WELL: The analogy between aqueous corrosion processes (e.g. galvanic couples) and cells / batteries is illuminating but limited. The cathodic reaction in galvanic corrosion is usually oxygen reduction or hydrogen evolution, not metal deposition. To predict galvanic corrosion of couples in seawater, we use the table of “Galvanic Series of some commercial metals and alloys in seawater” that. Slide30: EXAMPLES (from Fontana): A yacht with a Monel hull and steel rivets became unseaworthy because of rapid corrosion of the rivets. Severe attack occurred on aluminum tubing connected to brass return bends. Domestic hot-water tanks made of steel fail where copper tubing is connected to the tank. Pump shafts and valve stems made of steel or more corrosion-resistant materials fail because of contact with graphite packing.Slide32: Galvanic corrosion of painted steel auto body panel in contact with stainless steel wheel opening molding.Slide33: Moisture, etc.Slide34: Statue of LibertySlide35: Surface oxides (e.g., “rust”) are very important in galvanic corrosion: bare metal is a better cathode than oxide-covered metal; oxide interferes with hydrogen evolution and impedes oxygen diffusion; oxide puts an additional electrical resistance in the electrochemical circuit.Slide36: Oxide film effects: In standard EMF series, Al is more active than Zn (-1.662 V versus -0.763 V); we might expect that in a Zn-Al couple the Al would be anodic to the Zn. NOT SO! The Al2O3 film makes the Al more noble, so that Zn is anodic to it and actually protects it when coupled to it in solution (see “Galvanic Series in Seawater”). The oxide film on stainless steel is electrically insulating and impedes the charge flow between galvanic couples. The oxide film on copper is easily reduced. The resulting exposed metal is an efficient cathode. Oxygen is readily reduced there. Galvanic couples with copper can be very corrosive. Slide37: Note: diffusion & reduction of O2 often control galvanic corrosion, a large cathode area relative to the anode can be disastrous; such effects common at joints, where structures/components may be joined together with a different metal. Slide38: Effects of area relationship on corrosion of rivets (steel-copper couple) in seawater for 15 months.Slide39: Discuss: Two different metals of approximately the same area are joined to form a galvanic couple in a corrosive solution; we are to reduce the corrosion by coating (e.g., painting) one component of the couple. Do we coat the anode or the cathode?Slide40: Example … Slide43: Generally … Galvanic corrosion is under cathodic control … if we reduce the area of the Cathode (by coating, etc.) we reduce the corrosion; if we reduce the area of the Anode, corrosion will continue at the same rate but over a smaller area, so perforation etc. will occur sooner. TO REDUCE GALVANIC CORROSION BY COATINGS, THE MORE CORROSION-RESISTANT (i.e. THE MORE NOBLE OR CATHODIC) COMPONENT OF THE COUPLE IS COATED.Slide44: CATHODIC PROTECTION To reduce metallic corrosion, the component can made the CATHODE of a galvanic cell (a) by impressing an electric current from an external power source.Slide45: (b) by connecting the component to a SACRIFICIAL ANODE … Slide46: Cathodic protection by: Impressed current Sacrificial anodes …Slide47: ZINC PLATING (“ GALVANIZING”) Steel sheeting is coated with zinc by hot-dipping in the molten metal, by heating with zinc dust (“Sherardizing”), etc. The Zn coating acts as a sacrificial anode... at the inevitable imperfections, holes, etc., zinc dissolves preferentially, deposits loose, flocculant Zn(OH)2 from aqueous solution. Slide48: Protection continues as long as enough Zn is left ... if large enough areas of steel are exposed steel corrosion will occur usually at the middle of the exposed area.Slide49: If the temperature >60C, the Zn (OH)2 changes from a loose to a hard, compact form. This MAY change the polarity of the steel/Zn couple by making the Zn more noble than the steel; this CAN lead to rapid failure of the steel. NOTE: Galvanized steel should only be used in pH range 6 - 12.5.. ready dissolution of Zn in acids and alkalis quickly removes protection outside the range.Slide50: CADMIUM PLATING … similar action on steels to zinc plating: galvanic E less than for Zn; more protective than Zn in marine environments (chloride less soluble than ZnCl2- gives more protective coat); better than zinc in humid conditions indoors; used less and less because Cd is toxic TIN PLATING … different action from Zn or Cd; Sn is CATHODIC to steel; “pinhole” corrosion can occur at imperfections in tin plate.Slide51: Tin plate commonly used on steel cans for foodstuffs. Organic acids in foods, fruit juices etc., complex Sn2+ very readily ... lower potential, make tin anodic to steel.Slide52: Also, efficiency of Sn (and Fe) for H2 evolution poor; in O2-starved environment inside a food can, only possible cathodic reaction is H2 evolution; if evolution rate slow, the corrosion rate is slow (tins don’t explode very often). NOTE: Galvanic corrosion can occur without components of different metals actually being in electrical contact;Slide53: e.g. if soft water containing CO2 (i.e. slightly acid from carbonic acid) flows through copper pipes into a galvanized tank, copper ions will deposit on the zinc as metal: Cu2+ + Zn Cu + Zn2+ The Cu is an efficient cathode and will rapidly destroy the Zn coating. MINIMIZE GALVANIC CORROSION: MINIMIZE GALVANIC CORROSION Select metals as close together as possible in galvanic series; Avoid small-anode/large-cathode combinations . . . choose fasteners of more noble materials; Insulate dissimilar metals (e.g., sleeve bolts in flange joints, as well as use insulating washers); Apply coatings carefully, keep in good condition (esp. those on anodes); Add inhibitors, if possible, to environment; Avoid threaded joints where possible; Design for anodic member (make thicker, easily replaceable, etc.); Install a third metal that is anodic to BOTH in the couple. You do not have the permission to view this presentation. In order to view it, please contact the author of the presentation.
UN1001 Galvanic Corrosion Cubemiddle Download Post to : URL : Related Presentations : Share Add to Flag Embed Email Send to Blogs and Networks Add to Favorites Add to Channel Uploaded from authorPOINTLite Insert YouTube videos in PowerPont slides with aS Desktop Copy embed code: (To copy code, click on the text box) Embed: URL: Thumbnail: WordPress Embed Customize Embed The presentation is successfully added In Your Favorites. Views: 3405 Category: Entertainment License: All Rights Reserved Like it (3) Dislike it (1) Added: January 02, 2008 This Presentation is Public Favorites: 1 Presentation Description No description available. Comments Posting comment... By: durvesh16 (4 month(s) ago) wow great ppt Saving..... Post Reply Close Saving..... Edit Comment Close By: anilshegaon (12 month(s) ago) Very Well described and nicely put all the data in the presentation. Please send the said presentation to anilshegaon@yahoo.co.in With Warm Reagrds Anil Saving..... Post Reply Close Saving..... Edit Comment Close By: sudhirmaingi1974 (38 month(s) ago) Hello friend.. I m SUDHIR KUMAR working as lecturer in chemistry in kendriya vidyalaya vv nagar anand . I like very much your work on corrosion. Kindly send it to me at sudhir_maingi@rediffmail.com. Saving..... Post Reply Close Saving..... Edit Comment Close Premium member Presentation Transcript UN1001: REACTOR CHEMISTRY AND CORROSION Section 4: Galvanic Corrosion: UN1001: REACTOR CHEMISTRY AND CORROSION Section 4: Galvanic Corrosion By D.H. Lister & W.G. Cook Department of Chemical Engineering University of New BrunswickThe Eight Forms of Corrosion: The Eight Forms of Corrosion Uniform attack (general corrosion); Galvanic corrosion; Crevice corrosion; Pitting; Intergraular attack (“IGA”); Selective leaching; Flow-Accelerated Corrosion; Stress corrosion cracking (“SCC”) Slide3: Remember - electrochemistry basics in aqueous solution: metal dissolution is ANODIC: M Mn+ + n e- (e.g. Fe Fe 2+ + 2 e-) Slide4: and there are several possible CATHODIC reactions: hydrogen evolution (acids) 2 H+ + 2 e- H2 oxygen reduction (acids) O2 + 4H+ + 4 e- 2 H2O oxygen reduction (neutral or base) O2 + 2 H2O + 4 e- 4 OH- metal ion reduction M3+ + e- M2+ metal deposition M+ + e- M Note: More than one oxidation and more than one reduction reaction can occur during corrosion.Slide5: MULTIPLE CATHODIC REACTIONS ARE IMPORTANT. Thus, metals tend to dissolve more readily in aerated acids than in pure, de-aerated acid: In aerated acids, oxygen reduction AND hydrogen evolution can occur simultaneously: 2 H+ + 2 e- H2 O2 + 4H+ + 4 e- 2 H2O Also, an oxidizer, such as ferric ion, as an impurity in commercial acids makes them much more corrosive than pure acids because of the extra cathodic reaction that may occur: Fe3+ + e- Fe2+Slide6: Note: corrosion in sea water (or fresh water) is usually governed by oxygen reduction. If water is de-aerated, it becomes much less corrosive because the main reaction: O2 + 2 H2O + 4 e- 4 OH- can no longer occur. The cathodic reaction in absence of oxygen is hydrogen evolution: 2 H+ + 2 e- H2Slide7: REMEMBER: the metal dissolution reaction (corrosion) must always be balanced by one or more reduction reactions: For example, in neutral or alkaline water: 2 Fe 2 Fe2+ + 4 e- + O2 + 2 H2O + 4 e- 4 OH- 2 Fe + O2 + 2 H2O 2 Fe2+ + 4 OH- Fe2+ hydrolyses and precipitates, and is then oxidised to rust: 2 Fe(OH)2 ↓ + 1/2 O2 + H2O → 2 Fe(OH)3 Slide8: What about iron in a copper solution? Fe Fe2+ + 2 e- Cu2+ + 2 e- Cu Fe + Cu2+ Fe2+ + Cu (the old “nail in copper sulphate” trick!) clearly, the iron wants to be in solution more than the copper. the copper is more NOBLE than the iron; the iron is more ACTIVE than the copper. GALVANIC SERIES: A metal in contact with a solution establishes a POTENTIAL with respect to the solution How would we measure the potential difference Em - Es? GALVANIC SERIESSlide10: Em - Es cannot be measured, we can only measure the difference between it and Em - Es for another metal: (Em1 - Es) - (Em2 - Es) = Em1 - Em2 Slide11: CHANGES in potential of one electrode can be measured if the other electrode does not change, i.e. if it is a reference electrode. There are several reference electrodes which are constant so long as no current is drawn from them; Potentials relative to a reference electrode are therefore measured with meters (e.g. milli-voltmeters) of high impedance.Slide13: A metal in contact with a solution of its own ions at unit activity (thermodynamic concentration) establishes fixed potential differences with respect to every other metal in the same condition OF EQUILIBRIUM (potentials are reversible); THEREFORE, we can set up a series of standard electrode potentials with respect to some reference electrode; The standard hydrogen electrode (SHE) is chosen to have a potential of zero at 25C.Slide15: This has the accepted sign convention; however, some workers use opposite sign convention. These potentials are listed in accordance with the Stockholm Convention. See J. O’M. Bockris and A. K. N. Reddy, Modern Electrochemistry, Plenum Press, New York, 2002 COMMON REFERENCE ELECTRODES: COMMON REFERENCE ELECTRODES Ag(s)/AgCl(s) in 0.1 M KCl: + 0.288 V (SHE) in sat. KCl: +0.192 V (SHE) Cu(s)/Cu SO4 (saturated): + 0.316 V (SHE) Hg(s)/ Hg2Cl2(s) in 0.1 M KCl: + 0.334 V (SHE) in sat. KCl: +0.242 V (SHE) Slide17: By coupling two reversible electrodes together, we get a fixed potential difference: e.g. Ag / Ag+ - Cu2+ / Cu = 0.799 V - 0.337 V = 0.462 V (Discuss the possibility of making a reversible electrode out of an alloy such as brass.) Slide18: Note: If we drew current from two such electrodes (reversible Ag, Cu) THEY WOULD NO LONGER BE AT EQUILIBRIUM. THE REVERSIBILITY WOULD BE DESTROYED. silver would be deposited more than silver ions would be formed; copper ions would be formed more than copper would be deposited;Slide19: (remember, equilibrium or reversibility at an electrode means the rate of the forward reaction equals the rate of the back reaction). Another note: Corroding metals are not at equilibrium NOR are they usually in contact with unit activity of their own ions. THEREFORE the EMF series is an ideal system, which may be used as an indicator for practical situations. Slide20: IN GENERAL, as a rough guide: any metal in the EMF series will displace from solution any metal above it e.g. Fe displaces Cu from CuSO4 solution Zn displaces H2 from acid solution. BUT passivation of some metals alters its behavior; Slide21: Passivation is the formation of a very protective oxide layer that makes the metal more noble than it otherwise would be. e.g. Cr is a fairly reactive element, but Cr metal is usually passivated and cathodic to most common metals (hence chrome plating).Slide22: Galvanic corrosion MAY arise when dissimilar metals are in contact in aqueous solution. The potential difference between them will initiate attack, the corrosion rate depends on the surface reactions of (usually) both metals (i.e. we usually consider galvanic COUPLES of just two metals). Slide23: Galvanic potentials are made use of in batteries, e.g. the Daniel cell. In the Daniel cell, the zinc electrode is 1.1V negative with respect to the copper electrode. Which is the anode, the cathode? Which way does the electrical current flow?Slide24: The sign of the voltage on the Daniel cell indicates that, upon placing a load on the cell, a spontaneous de-electronation will occur on the zinc electrode; and electronation, on the copper electrode. Slide25: A Dry Cell: Dry cells are electrochemical energy storers in which the electrolyte is immobilized in the form of a paste. A typical dry cell is the Leclanche cell. A schematic diagram of this cell is shown below. The reactions occurring in the cell during discharge are: at the anode: Zn Zn2+ + 2 e- at the cathode: 2 MnO2 + 2 H3O+ + 2 e- Mn2O3 + 3 H2O Or 2 MnO2 + H2O + 2 e- Mn2O3 + 2 OH- Slide27: Since hydroxide ions are produced during working (because H3O+ is consumed), the following irreversible side reactions occur: OH- + NH4+ H2O + NH3 Zn2+ + 2 NH3 + 2 Cl- Zn(NH3)2Cl2 Zn2+ + 2 OH- ZnO + H2O ZnO + Mn2O3 Mn2O3 ZnO Owing to the above reactions, the cell is only partially rechargeable and this to such a small extent that it is never done in practice. Slide28: NOTE WELL: The analogy between aqueous corrosion processes (e.g. galvanic couples) and cells / batteries is illuminating but limited. The cathodic reaction in galvanic corrosion is usually oxygen reduction or hydrogen evolution, not metal deposition. To predict galvanic corrosion of couples in seawater, we use the table of “Galvanic Series of some commercial metals and alloys in seawater” that. Slide30: EXAMPLES (from Fontana): A yacht with a Monel hull and steel rivets became unseaworthy because of rapid corrosion of the rivets. Severe attack occurred on aluminum tubing connected to brass return bends. Domestic hot-water tanks made of steel fail where copper tubing is connected to the tank. Pump shafts and valve stems made of steel or more corrosion-resistant materials fail because of contact with graphite packing.Slide32: Galvanic corrosion of painted steel auto body panel in contact with stainless steel wheel opening molding.Slide33: Moisture, etc.Slide34: Statue of LibertySlide35: Surface oxides (e.g., “rust”) are very important in galvanic corrosion: bare metal is a better cathode than oxide-covered metal; oxide interferes with hydrogen evolution and impedes oxygen diffusion; oxide puts an additional electrical resistance in the electrochemical circuit.Slide36: Oxide film effects: In standard EMF series, Al is more active than Zn (-1.662 V versus -0.763 V); we might expect that in a Zn-Al couple the Al would be anodic to the Zn. NOT SO! The Al2O3 film makes the Al more noble, so that Zn is anodic to it and actually protects it when coupled to it in solution (see “Galvanic Series in Seawater”). The oxide film on stainless steel is electrically insulating and impedes the charge flow between galvanic couples. The oxide film on copper is easily reduced. The resulting exposed metal is an efficient cathode. Oxygen is readily reduced there. Galvanic couples with copper can be very corrosive. Slide37: Note: diffusion & reduction of O2 often control galvanic corrosion, a large cathode area relative to the anode can be disastrous; such effects common at joints, where structures/components may be joined together with a different metal. Slide38: Effects of area relationship on corrosion of rivets (steel-copper couple) in seawater for 15 months.Slide39: Discuss: Two different metals of approximately the same area are joined to form a galvanic couple in a corrosive solution; we are to reduce the corrosion by coating (e.g., painting) one component of the couple. Do we coat the anode or the cathode?Slide40: Example … Slide43: Generally … Galvanic corrosion is under cathodic control … if we reduce the area of the Cathode (by coating, etc.) we reduce the corrosion; if we reduce the area of the Anode, corrosion will continue at the same rate but over a smaller area, so perforation etc. will occur sooner. TO REDUCE GALVANIC CORROSION BY COATINGS, THE MORE CORROSION-RESISTANT (i.e. THE MORE NOBLE OR CATHODIC) COMPONENT OF THE COUPLE IS COATED.Slide44: CATHODIC PROTECTION To reduce metallic corrosion, the component can made the CATHODE of a galvanic cell (a) by impressing an electric current from an external power source.Slide45: (b) by connecting the component to a SACRIFICIAL ANODE … Slide46: Cathodic protection by: Impressed current Sacrificial anodes …Slide47: ZINC PLATING (“ GALVANIZING”) Steel sheeting is coated with zinc by hot-dipping in the molten metal, by heating with zinc dust (“Sherardizing”), etc. The Zn coating acts as a sacrificial anode... at the inevitable imperfections, holes, etc., zinc dissolves preferentially, deposits loose, flocculant Zn(OH)2 from aqueous solution. Slide48: Protection continues as long as enough Zn is left ... if large enough areas of steel are exposed steel corrosion will occur usually at the middle of the exposed area.Slide49: If the temperature >60C, the Zn (OH)2 changes from a loose to a hard, compact form. This MAY change the polarity of the steel/Zn couple by making the Zn more noble than the steel; this CAN lead to rapid failure of the steel. NOTE: Galvanized steel should only be used in pH range 6 - 12.5.. ready dissolution of Zn in acids and alkalis quickly removes protection outside the range.Slide50: CADMIUM PLATING … similar action on steels to zinc plating: galvanic E less than for Zn; more protective than Zn in marine environments (chloride less soluble than ZnCl2- gives more protective coat); better than zinc in humid conditions indoors; used less and less because Cd is toxic TIN PLATING … different action from Zn or Cd; Sn is CATHODIC to steel; “pinhole” corrosion can occur at imperfections in tin plate.Slide51: Tin plate commonly used on steel cans for foodstuffs. Organic acids in foods, fruit juices etc., complex Sn2+ very readily ... lower potential, make tin anodic to steel.Slide52: Also, efficiency of Sn (and Fe) for H2 evolution poor; in O2-starved environment inside a food can, only possible cathodic reaction is H2 evolution; if evolution rate slow, the corrosion rate is slow (tins don’t explode very often). NOTE: Galvanic corrosion can occur without components of different metals actually being in electrical contact;Slide53: e.g. if soft water containing CO2 (i.e. slightly acid from carbonic acid) flows through copper pipes into a galvanized tank, copper ions will deposit on the zinc as metal: Cu2+ + Zn Cu + Zn2+ The Cu is an efficient cathode and will rapidly destroy the Zn coating. MINIMIZE GALVANIC CORROSION: MINIMIZE GALVANIC CORROSION Select metals as close together as possible in galvanic series; Avoid small-anode/large-cathode combinations . . . choose fasteners of more noble materials; Insulate dissimilar metals (e.g., sleeve bolts in flange joints, as well as use insulating washers); Apply coatings carefully, keep in good condition (esp. those on anodes); Add inhibitors, if possible, to environment; Avoid threaded joints where possible; Design for anodic member (make thicker, easily replaceable, etc.); Install a third metal that is anodic to BOTH in the couple.