Title: 4.0 CORROSION PREVENTION
14.0 CORROSION PREVENTION
- MATERIAL SELECTION
- ALTERATION OF ENVIRONMENT
- PROPER DESIGN
- CATHODIC PROTECTION
- ANODIC PROTECTION
- COATINGS WRAPPING
2- (1) MATERIAL SELECTION
- (selection of proper material for a
particular corrosive service)
- Metallic metal and alloy
- Nonmetallic rubbers (natural and synthetic),
plastics, ceramics, carbon and graphite, and wood
3Metals and Alloys
No Environment Proper material
1 Nitric acid Stainless steels
2 Caustic Nickel and nickel alloys
3 Hydrofluoric acid Monel (Ni-Cu)
4 Hot hydrochloric acid Hastelloys (Ni-Cr-Mo) (Chlorimets)
5 Dilute sulfuric acid Lead
4No Environment Proper material
6 Nonstaining atmospheric exposure Aluminium
7 Distilled water Tin
8 Hot strong oxidizing solution Titanium
9 Ultimate resistance Tantalum
10 Concentrated sulfuric acid Steel
5E.g Stainless Steels
Stainless steels are iron base alloys that
contain a minimum of approximately 11 Cr, the
amount needed to prevent the formation of rust in
unpolluted atmosphere.
Dissolution rate, cm/sec
wt. Cr
6Alloying elements of stainless steel
- Other than Ni, Cr and C, the following alloying
elements may also present in stainless steel Mo,
N, Si, Mn, Cu, Ti, Nb, Ta and/or W. - Main alloying elements (Cr, Ni and C)
- 1. Chromium
- Minimum concentration of Cr in a
- stainless steel is 12-14wt.
- Structure BCC (ferrite forming element)
- Note that the affinity of Cr to form
Cr-carbides is very - high. Chromium carbide formation along
grain - boundaries may induce intergranular
corrosion.
7Binary diagram of Fe-Cr
Sigma phase formation which is initially formed
at grain boundaries has to be avoided because it
will increase hardness, decrease ductility and
notch toughness as well as reduce corrosion
resistance.
8- 2. Nickel
- Structure FCC (austenite forming
element/stabilize austenitic structure) - Added to produce austenitic or duplex
stainless steels. These materials possess
excellent ductility, formability and toughness as
well as weld-ability. - Nickel improves mechanical properties of
stainless steels servicing at high temperatures. - Nickel increases aqueous corrosion
resistance of materials. -
9Ternary diagram of Fe-Cr-Ni at 6500 and 10000C
AISI American Iron and Steel Institute
10Anodic polarization curves of Cr, Ni and Fe in 1
N H2SO4 solution
11Influence of Cr on corrosion resistance of iron
base alloy
12Influence of Ni on corrosion resistance of iron
base alloy
13Influence of Cr on iron base alloy containing
8.3-9.8wt.Ni
14- 3. Carbon
- Very strong austenite forming element (30x
more effective than Ni). I.e. if austenitic
stainless steel 18Cr-8Ni contains 0.007C, its
structure will convert to ferritic structure.
However the concentration of carbon is usually
limited to 0.08C (normal stainless steels) and
0.03C (low carbon stainless steels to avoid
sensitization during welding).
15Minor alloying elements
- Manganese
- Austenitic forming element. When necessary can
be used to substitute Ni. Concentration of Mn in
stainless steel is usually 2-3. - Molybdenum
- Ferritic forming element. Added to increase
pitting corrosion resistance of stainless steel
(2-4). - Molybdenum addition has to be followed by
decreasing chromium concentration (i.e. in 18-8SS
has to be decreased down to 16-18) and
increasing nickel concentration (i.e. has to be
increased up to 10-14). - Improves mechanical properties of stainless
steel at high temperature. Increase aqueous
corrosion resistance of material exposed in
reducing acid.
16- Tungsten
- Is added to increase the strength and
toughness of martensitic stainless steel. - Nitrogen (up to 0.25)
- Stabilize austenitic structure. Increases
strength and corrosion resistance. Increases weld
ability of duplex SS. - Titanium, Niobium and Tantalum
- To stabilize stainless steel by reducing
susceptibility of the material to intergranular
corrosion. Ti addition gt 5xC. TaNb addition gt
10xC.
17- Copper
- Is added to increase corrosion resistance of
stainless steel exposed in environment containing
sulfuric acid. - Silicon
- Reduce susceptibility of SS to pitting and
crevice corrosion as well as SCC.
18Influence of alloying elements on pitting
corrosion resistance of stainless steels
19Influence of alloying elements on crevice
corrosion resistance of stainless steels
20Influence of alloying elements on SCC resistance
of stainless steels
21Five basic types of stainless steels
- Austenitic - Susceptible to SCC. Can be hardened
by only by cold working. Good toughness and
formability, easily to be welded and high
corrosion resistance. Nonmagnetic except after
excess cold working due to martensitic formation. - Martensitic - Application when high mechanical
strength and wear resistance combined with some
degree of corrosion resistance are required.
Typical application include steam turbine blades,
valves body and seats, bolts and screws, springs,
knives, surgical instruments, and chemical
engineering equipment. - Ferritic - Higher resistance to SCC than
austenitic SS. Tend to be notch sensitive and are
susceptible to embrittlement during welding. Not
recommended for service above 3000C because they
will loss their room temperature ductility.
22- Duplex (austenitic ferritic) has enhanced
resistance to SCC with corrosion resistance
performance similar to AISI 316 SS. Has higher
tensile strengths than the austenitic type, are
slightly less easy to form and have weld ability
similar to the austenitic stainless steel. Can be
considered as combining many of the best features
of both the austenitic and ferritic types. Suffer
a loss impact strength if held for extended
periods at high temperatures above 3000C. - Precipitation hardening - Have the highest
strength but require proper heat-treatment to
develop the correct combination of strength and
corrosion resistance. To be used for specialized
application where high strength together with
good corrosion resistance is required.
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31Stress Corrosion Cracking of Stainless Steel
- Stress corrosion cracking (SCC) is defined as
crack nucleation and propagation in stainless
steel caused by synergistic action of tensile
stress, either constant or slightly changing with
time, together with crack tip chemical reactions
or other environment-induced crack tip effect. - SCC failure is a brittle failure at relatively
low constant tensile stress of an alloy exposed
in a specific corrosive environment. - However the final fracture because of overload of
remaining load-bearing section is no longer SCC.
32- Three conditions must be present simultaneously
to produce SCC - - a critical environment
- - a susceptible alloy
- - some component of tensile stress
33Pure metals are more resistance to SCC but not
immune and susceptibility increases with strength
Tensile stress is below yield point
Susceptible material
Tensile stress
Stress corrosion cracking
Corrosive environment
Corrosive environment is often specific to the
alloy system
34Typical micro cracks formed during SCC of
sensitized AISI 304 SS
Surface morphology
35Example of crack propagation during transgranular
stress corrosion cracking (TGSCC) brass
36Example of crack propagation during intergranular
stress corrosion cracking (IGSCC) ASTM A245
carbon steel
37Fracture surface of intergranular SCC on carbon
steel in hot nitric solution
Fracture surface of transgranular SCC on
austenitic stainless steel in hot chloride
solution
38Fracture surface due to local stress has reached
its tensile strength value on the remaining
section
Fracture surface due to intergranular SCC
39Electrochemical effect
Usual region for TGSCC, mostly is initiated by
pitting corrosion (transgranular cracking
propagation needs higher energy)
pitting
Zone 1
passive
cracking zones
Zone 2
Usual region for IGSCC, SCC usually occurs where
the passive film is relatively weak
active
40- Note that non-susceptible alloy-environment
combinations, will not crack the alloy even if
held in one of the potential zones. - Temperature and solution composition (including
pH, dissolved oxidizers, aggressive ions and
inhibitors or passivators) can modify the anodic
polarization behavior to permit SCC. - Susceptibility to SCC cannot be predicted solely
from the anodic polarization curve.
41Models of stress corrosion cracking
- Slip step dissolution model
- Discontinuous intergranular crack growth
- Crack nucleation by rows of corrosion
micro-tunnels - Absorption induced cleavage
- Surface mobility (atoms migrate out of the crack
tips) - Hydrogen embrittlement?HIC
42- Control/prevention
- Reduce applied stress level
- Remove residual tensile stress (internal stress)
- Lowering oxidizing agent and/or critical species
from the environment - Add inhibitor
- Use more resistant alloys
- Cathodic protection
432. Alteration of Environment
- Typical changes in medium are
- Lowering temperature but there are cases where
increasing T decreases attack. E.g hot, fresh or
salt water is raised to boiling T and result in
decreasing O2 solubility with T. - Decreasing velocity exception metals alloys
that passivate (e.g stainless steel) generally
have better resistance to flowing mediums than
stagnant. Avoid very high velocity because of
erosion-corrosion effects.
44- Removing oxygen or oxidizers e.g boiler
feedwater was deaerated by passing it thru a
large mass of scrap steel. Modern practice
vacuum treatment, inert gas sparging, or thru the
use of oxygen scavengers. However, not
recommended for active-passive metals or alloys.
These materials require oxidizers to form
protective oxide films. - Changing concentration higher concentration of
acid has higher amount of active species (H
ions). However, for materials that exhibit
passivity, effect is normally negligible.
45Environment factors affecting corrosion design
- Dust particles and man-made pollution CO, NO,
methane, etc. - Temperature high T high humidity accelerates
corrosion. - Rainfall excess washes corrosive materials and
debris but scarce may leave water droplets. - Proximity to sea
- Air pollution NaCl, SO2, sulfurous acid, etc.
- Humidity cause condensation.
463. Design Dos Donts
- Wall thickness allowance to accommodate for
corrosion effect. - Avoid excessive mechanical stresses and stress
concentrations in components exposed to corrosive
mediums. Esp when using materials susceptible to
SCC. - Avoid galvanic contact / electrical contact
between dissimilar metals to prevent galvanic
corrosion. - Avoid sharp bends in piping systems when high
velocities and/or solid in suspension are
involved erosion corrosion. - Avoid crevices e.g weld rather than rivet tanks
and other containers, proper trimming of gasket,
etc.
47- Avoid sharp corners paint tends to be thinner
at sharp corners and often starts to fail. - Provide for easy drainage (esp tanks) avoid
remaining liquids collect at bottom. E.g steel is
resistant against concentrated sulfuric acid. But
if remaining liquid is exposed to air, acid tend
to absorb moisture, resulting in dilution and
rapid attack occurs. - Avoid hot spots during heat transfer operations
localized heating and high corrosion rates. Hot
spots also tend to produce stresses SCC
failures. - Design to exclude air except for active-passive
metals and alloys coz they require O2 for
protective films. - Most general rule AVOID HETEROGENEITY!!!
484. Protective Coatings / Wrapping
- Provide barrier between metal and environment.
- Coatings may act as sacrificial anode or release
substance that inhibit corrosive attack on
substrate. - Metal coatings
- Noble silver, copper, nickel, Cr, Sn, Pb on
steel. Should be free of pores/discontinuity coz
creates small anode-large cathode leading to
rapid attack at the damaged areas. - Sacrificial Zn, Al, Cd on steel. Exposed
substrate will be cathodic will be protected. - Application hot dipping, flame spraying,
cladding, electroplating, vapor deposition, etc.
49- Surface modification to structure or
composition by use of directed energy or particle
beams. E.g ion implantation and laser processing. - Inorganic coating cement coatings, glass
coatings, ceramic coatings, chemical conversion
coatings. - Chemical conversion anodizing, phosphatizing,
oxide coating, chromate. - Organic coating paints, lacquers, varnishes.
Coating liquid generally consists of solvent,
resin and pigment. The resin provides chemical
and corrosion resistance, and pigments may also
have corrosion inhibition functions.
505. Cathodic and Anodic Protection5.1 Cathodic
Protection
- Cathodic Protection (CP) was employed before the
science of electrochemistry had been developed - CP is achieved by supplying electrons to the
metal structure to be protected. (M Mn
ne) and (2H 2e H2) - Examination of equation indicates the addition of
electrons to the structure will tend to suppress
metal dissolution and increase the rate of
hydrogen dissolution - If current is considered to flow from () to (-),
then a structured is protected if current enters
it from the electrolyte - Conversely, accelerated corrosion occurs if
current passes from the metal to the electrolyte,
this current convention has been adopted in
cathodic protection technology and is used here
for consistency
51- There 2 ways to cathodically protect a structure
- (i) by an external power supply
- (ii) by appropriate galvanic coupling
52- Figure illustrates CP by impressed current
- Here, an external dc power supply is connected to
an underground tank, the negative terminal of the
power supply is connected to the tank, and the
positive terminal to an inert anode such as
graphite or Duriron. - The electric leads to the tank and inert the
electrode are carefully insulated to prevent
current leakage - The anode is usually surrounded by backfill
consisting of coke breeze, gypsum or bentonite
which improves electric contact between the anode
and the surrounding soil. - In figure, current passes to the metallic
structure and corrosion is suppressed
53- CP by galvanic coupling to Mg is shown in Fig
6.2 - Mg is anodic with respect to steel and corrodes
preferentially when galvanic coupled The anode
in this case is called a sacrificial anode since
it is consumed during the protection of the steel
structure - CP using sacrificial anodes can also be used to
protect buries pipelines shown Fig 6.3. the
anodes are spaced along the pipe to ensure
uniform current distribution
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565.2 Anodic Protection
- In contrast to CP, anodic protection (AP) is
relatively new - This technique was developed using electrode
kinetics principles and is somewhat difficult to
describe without introducing advanced concepts of
electrochemical theory - Simply, AP is based is based on the formation of
a protective film on metals by externally applied
anodic currents. - This usually except for metals with
active-passive transitions such as Ni, Fe, Cr, Ti
and their alloys - If carefully controlled anodic currents are
applied to these materials, they are passivated
and the rate of metal dissolution is decreased - To anodically protect a structure, a device
called a potentiostat is required - A potentiostat is an electronic device that
maintains a metal at a constant potential with
respect to a reference electrode.
57- The potentiostat has three terminals, one
connected to the tank, another to an auxiliary
cathode (a platinum or platinum-clad electrode)
and the third to a reference electrode (e.g.
calomel cell) - In operation, the potentiostat maintains a
constant potential between the tank and the
reference electrode - The optimum potential for protection is
determined by electrochemical measurements
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