1/65
Looks like no tags are added yet.
Name | Mastery | Learn | Test | Matching | Spaced | Call with Kai |
|---|
No analytics yet
Send a link to your students to track their progress
To change corrosion rates
reduce/accelerate either the anodic or cathodic reaction
Environmental effects can change reaction
Oxygen/Oxidizers
For most metals that do not form an unreactive oxide layer (pink)
Adding INCREASES the corrosion rate
For metals that do not form an unreactive oxide layer, there is a point where additional oxygen/oxidizer has no effect (blue)
For metals originally exist with the unreactive oxide film, shift to active can occur IF very powerful oxidizers are added (purple)
For most metals that do not form an unreactive oxide layer
Adding oxygen or oxidizers INCREASES the corrosion rate
For metals that do not form an unreactive oxide layer, there is a point where additional oxygen/oxidizer has no effect (blue)
This occurs when the oxide layer has formed and corrosive attack can no longer occur (get through the oxide)
If the process controlled by reaction series
then velocity has no effect
For reaction series to control, species must first attach, then electron transfer, then release
If metal readily forms oxide film
then slow velocities keep corrosive ions near the surface, preventing film formation, while fast velocities form more oxides (pink)
Some metals form large bulk films
but only weakly attached.
Prior to velocity breaking/peeling film, corrosion barely occurs. Once velocity has broken the adhered film, corrosion increases (red)
Increasing temperature
Increases corrosion rates
Some metals see a gradual increase (Blue)
Some metal see a minimal change, followed by a rapid increase
Concentration of corrosive Ions
Metals with an unreactive oxide film can withstand higher concentrations before the ions overwhelm the film (pink)
Film may also become soluble in solution at high concentrations
Concentration of Corrosive ions
Most common with acids; As acid concentration increases, hydrogen ions increase. At a certain point, ionization of hydrogen is reduced, reducing the amount of hydrogen available for reaction thus reducing corrosion create (blue)
H+ automatically becomes H2
Uniform Attack
Metals is evenly attacked across the entire surface
Metal thins until piece fails
Reaction sites move around surface, creating uniform disintegration
Greatest destruction of metal on a tonnage basis
Not a great technical issue
Lifespan determined by comparison to tests
Can be reduced by coatings, corrosion inhibitors, or cathodic protection
Localized Corrosion- Uniform Attack
Anodes and cathodes become fixed
Leads to formation of geometrical constrained concentrations points, which prevent removal of corrosive ions, allowing continued attack
Corrosion "focuses" on those spots, leading to faster disintegration in that region and failure at those points
Crevice Corrosion
Shielded areas on metal surfaces are exposed to corrosive environment
Ex. Bolt (there is a space the environment can get under the bolt above the metal- shielded)
Environment becomes stagnant
very narrow sites around a few thousands of inch, allow solution to enter but not leave
External surfaces protected because rate of oxygen reduction increases, leaving the external metal along
Usually occurs in chloride containing environments
Long incubation period of six months to one year before attack starts, but then accelerates after starting
It can be wielded to prevent crevice corrosion (wield the bolt down)
Avoid sharp corners and stagnate zones
Environment becomes stagnant- Crevice
Under a deposit, such as sand, dirt, solids out of solution, or under bolt heads and rivets, near gasket surfaces
Crevice
very narrow sites around a few thousands of inch, allow solution to enter but not leave
Crevice
Solution becomes depleted of oxygen, initially decreases the corrosion rate in the crevice
The metal is actively corroding, just very slowly, positive metal ions are collecting
At some point, those positive metal ions attract negative ions to migrate into this region
Negative ions increase, rate of metal dissolution increases, increasing the positive ions, increases the negative ion migration
Overall, the effect is to accelerate corrosion in an autocatalytic manner (once stated, cannot be stopped)
Pitting Corrosion
Localized corrosion resulting in holes in the metal
Small or large in diameter
Isolated (individual) or close together
Surface diameters is the same or less than the depth
Very destructive
Pitting Corrosion is Difficult
Difficult to detect because of small size AND that it is likely covered in corrosion products
Difficult to test for because of randomness in formation in same conditions, varying depths of the pits, and varying number of pits
Failure occurs with extreme suddenness- Pitting Corrosion
Minimal weight loss in entire structure but a stress concentration point was created, the "focused" stress to lead to failure
Pits grow
in the direction of gravity
Grow downwards from a horizontal surface
As with crevice corrosion, after starts, grows at increasing rate- Pitting Corrosion
Growth under the surface is more severe than surface damage indicates
Rapid dissolution of metal occurring- Type of anodic reaction- Pitting
(creates positive metal ions)
Migration of chloride ions into pit
Type of Anodic reaction- Pitting
counteract the positive metal charge
Switch to production of hydrogen ions
Type of anodic reaction- Pitting
(because chloride ions "left" the hydrogen behind to "join" the metal)
No oxygen reduction occurring in the pits
Oxygen reduction on metal surface
(with the abandoned hydrogen) surrounding pits protects other metal surfaces
Type of anodic reaction- Pitting
No mechanisms for start of pitting
that adequately explains pitting nucleation (formation)
Believed it occurs when a spot momentarily has a higher dissolution of metal, causing chloride ions to migrate, stimulating more metal dissolution
type of anodic reaction- pitting
Pitting most commonly occurs in
chloride containing solutions
Also occur with other halide ions, like bromide and hypochlorite's
Not so corrosive with fluorides and iodides
Oxidizing metals in conjunction with chlorides are especially bad, CuCl2, FeCl3, HgCl2
Nonoxidizing metals are less aggressive but still corrosive
NaCl and CaCl2
type of anodic reaction- pitting
Associated with stagnent conditions
Allows chloride ions "settle", thereby increasing pitting
Type of anodic reaction
Stress Corrosion Cracking (SCC)
Cracking caused by presence of a tensile (load) stress and a corrosive medium
Have a stress concentration point, like a pit
No general pattern
Special Type Corrosion Fatigue
Stress concentration point- SCC
Corrosive media enters pit/point and as stress is applied, point opens allowing more media in, which reacts with the fresh metal
Stress corrosion cracking
as little as 10% of yield strength (which is already measured from 2% strain)
corrosion by-products can- SCC
increase stress within the crack by crating "wedges", causing the crack tip to grow faster
Accelerates crack growth beyond what corrosion alone would cause
No general pattern SCC
Occurs in aqueous media, as well as in liquid metals, salts, and nonaqueous inorganic liquids
Oxidizers do increase stress corrosion cracking
Accelerated by increasing temperature
Corrosion Fatigue
Instead of an applied tensile stress, this is a cyclically applied tensile stress (applied, released, applied, released, in a cycle)
causes a reduction in fatigue due to the presence of a corrosive medium
Most pronounced at low stress frequencies
Have a greater contact time between the metal and the environment
Oxygen content, temperature, pH and solution affect corrosion fatigue
Hydrogen damaging
Mechanical Damage of a metal caused by the presence of, or interaction with, hydrogen
4 Types
Hydrogen Blistering
Hydrogen Embrittlement
Decarburization
Hydrogen Attack
Hydrogen Blistering
Hydrogen ions diffuse into metal and find a void
In void, combines with another hydrogen ion to form H2
The H2 can now NOT diffuse out
Concentration and pressure builds up, eventually resulting in rupture of the metal
The H2 pressure can build up to several hundred thousand atmospheres before rupture
Hydrogen Embrittlement
Hydrogen ions diffuse into metal and react with the metal
Forms a brittle, hydride compound
Destructive behavior is similar to stress-corrosion cracking, where hydride compound increase stress concentration, allows crack growth until failure
Main difference deals with the reactions
When specimen becomes more anodic, stress corrosion cracking (so more
M+ and e- produced)
Electrons flow FROM metal- Hydrogen embrittlement
increasing positive concentrations (M+), get stress corrosion cracking
Electron flow TO metal- Hydrogen Embrittlement
because of hydrogen bonding, hydrogen embrittlement
Decarburization
Removal of carbon from an alloy and occurs at high temperatures
Remove carbon precipitates, reduce the strength of the metal
Reaction of carbon with hydrogen forms methane
Cracking can occur when methane forms internally in voids
Chromium and molybdenum improve resistance because these carbides are more stable than iron carbides
Hydrogen Attack
Carbon in iron reacts with water vapor, forming carbon monoxide and hydrogen attack within the metal
Need high temperature for this to occur
Leaching
Removal of one element from a solid alloy by corrosion processes\
Is similar to pitting in that the overall dimension does not change appreciably
Removal of that element weakens the metal, causing it to become brittle
Often see holes AND color change, but if not examined closely, sudden failure can occur
Stagnant conditions favor leaching
Similar to pitting, small change greatly affect metal MAJOR difference- Leaching
with leaching, the holes can be anywhere, while with pitting, they only go with gravity
Dezincification- leaching- stagnant conditions
Removal of zinc from brass, leaving behind copper
Graphitization- leaching- stagnant conditions
Removal of iron (Fe) from gray cast iron, leaving behind graphite
Intergranular Corrosion
Usually occurs because boundary is slightly more reactive than grains, so usually, uniform corrosion dominates
Caused by impurities at the grain boundaries
Chromium is added to stainless steel for corrosion effects and mechanical behavior
Welds
A localized attack at adjacent to grain boundaries- Intergranular Corrosion
with relatively little corrosion of grains is intergranular corrosion
By just weakening the overall structure but over time, the grain boundary can be corrode enough that the grain falls out
Impurities at the grain boundaries
Enrichment of an alloying element
Depletion of an alloying element
Depletion of chromium near grain boundaries- Intergranular Corrosion
leads to intergranular corrosion
Chromium forms solid precipitates at grain, leaves adjacent areas (where there should be chromium) lower in chromium and more open to corrosion
Welds
is undisturbed
Because weld cools down quickly, elements cannot diffuse
Some distance from the weld (heat affected zone, HAZ) where heat transfer occurred, an alloying element precipitates out
When alloying element precipitates out, no corrosion protections exist
Stainless steels
High temperature solution treatment with quenching
High temperature ensures chromium carbide is dissolves
Quenching ensures rapid cooling so precipitates cannot form
Add elements to purposely form carbides
Titanium, Columbium, Tantalum have a strong affinity for carbon versus chromium
Combine with all carbons, preventing formation of chromium carbides
Lower carbon content to below 0.03%
Carbon formation is insufficient so intergranular precipitates cannot form
Difference between SS316 and SS316L
Erosion Corrosion
Acceleration or increase in rate of deterioration or attack on a metal because of relative movement between a corrosive fluid and the metal surface
Movement is rapid with mechanical wear and / or abrasion
Metal is removed as dissolved ions OR solid products are mechanically removed from surface
Characteristics of erosion corrosion
grooves, gullies, waves, rounded holes, valleys
Formed in directional pattern
Occur in a relatively short amount of time
All metals are susceptible
Films that form an unreactive oxide, if the oxide is damaged, increased corrosion and increased byproducts (peeled aways oxide film)
Metal that are soft are easily worn mechanically and ball or peel
All environments are potential problems for erosion corrosion
Gases, Aqueous solution, organic systems, liquid metals
All types of equipment subjected to moving fluids are susceptible
Piping systems, mainly in bends, elbows, and tees
Valves, pumps, blowers, propellers, impellers, baffles, agitators, and agitated vessels, heat exchanger tubing
Factors of Erosion Corrosion
Surface films
Velocity
Turbulence
Impingement
Surface Films
protective oxide films formed protect against corrosion but not against wear, and can be delaminated because of wear
Velocity
increasing velocity, especially from increased rate of flow, increase erosion corrosion
Turbulence
Greater agitation of liquid at metal surface, more dissolved solid that can form
Impingement
Fluid forced to change direction
Fretting
Corrosion occurring at constant areas between materials under load subjected to vibration and slip- Knee replacement example
Pits or grooves surrounded by corrosion products in common
Characteristics of fretting
Can occur in the atmosphere or in media not usually corrosive
Engine components, automotive parts, bolted parts, implants
Destruction of metallic components through the production of oxide debris
Leads to seizing and galling because of the loss of tolerance and loosing
Loosening allows excessive strain, leads to fatigue fracture
To get fretting, you need an
interface under load
Vibration or repeated relative motion
Load and motion must be sufficient to produce slip
slip
where you have small movement of a sliding nature
Only 10^-8 cm of relative motion is needed to cause fretting damage
Must be repeated- Continuous motion does not exhibit fretting
Ball Bearings
Ball Bearings
In sealed environment with low viscous fluid, do not get fretting; get a piece of dirt/dust in fluid, causes bearing to move differently, get fretting
Cavitation Corrosion
Formation and collapse of vapor bubbles in liquid near a metal surface
Hydraulic turbines, ship propellers, pump impellers, other high-velocity liquid flow with pressure changes
Production and collapse of bubbles that produce shockwaves with pressure as high as 60,000 lb/in^2 (psi)
Leads to plastic (irreversible) damage
Resemble pitting (deep holes) but holes are closely spaced and surface is distinctly roughened