INTERNAL CORROSION Flashcards

1
Q

Sweet corrosion

A

CARBON DIOXIDE CO2

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2
Q

may exist when fertilizers contact metal surface and may be inhibited using water.

A

AMMONIA NH3

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3
Q

it is often in the form of SCC. It can also be reduced by stress relieving storage tanks before exposure to this corrosive substance.

A

AMMONIA NH3

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4
Q

This is corrosion is controlled by the formation of iron carbonate on the metal surface which can cause pitting if the protective scale is damaged.

A

CARBON DIOXIDE CO2

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5
Q

In the presence of water, it may form carbonic acid (H2CO3) and the corrosion rate is affected by temperature, velocity, pressure, and pH.

A

CARBON DIOXIDE CO2

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6
Q

Damage that occurs at the solid/liquid interface under conditions of turbulent flow as a result of the formation and rapid collapse of cavities or bubbles within a liquid.

A

CAVITATION CORROSION

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7
Q

Remedies include changing vapor pressure and material selection.

A

CAVITATION CORROSION

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8
Q

This is caused by a greenish yellow gas or liquid which is utilized in water purification, bleaches, and mustard gas.

A

CHLORINE CL2

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9
Q

It is commonly used in swimming pools. It can attack iron, steel, aluminum, nickel, stainless steel, copper, and titanium but attack is minimized if corrodent kept dry but titanium it should be wet.

A

CHLORINE CL2

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10
Q

A conjoint action involving corrosion and erosion in the presence of a moving corrosive fluid or a material moving through the fluid leading to an accelerated loss of material.

A

EROSION CORROSION

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11
Q

This type of corrosion does not require the presence of a liquid electrolyte, but usually involves the presence of oxidizing and reducing gases which affect the formation of protective oxide scales.

A

HIGH TEMPERATURE

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12
Q

Some of the effects or issues related to this corrosion are nitriding, carburization, internal oxidation, hydrogen attack, and halide attack.

A

HIGH TEMPERATURE

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13
Q

this produces iron sulfide as a by-product and also damages metal by causing embrittlement to hard alloys and blistering to softer alloys.

A

HYDROGEN SULFIDE H2S

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14
Q

Unaffected by velocity. known as sour corrosion.

A

HYDROGEN SULFIDE H2S

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15
Q

One of the few that attacks glass, therefore the corrodent can only by stored in plastic or teflon containers.

A

HYDROGEN FLUORIDE HF

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16
Q

This is utilized to purify aluminum and uranium

A

HYDROGEN FLUORIDE HF

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17
Q

Similar to wet chlorine corrosion.

A

HYPCHLORITE

18
Q

It is encountered in bleaching, sanitizing, deodorizing, and waste treatment applications.

A

HYPOCHLORITE

19
Q

Sodium version called liquid bleach

Calcium version is solid called bleaching powder.

A

HYPOCHLORITE

20
Q

Lower temperatures will greatly reduce the corrosion rate of this corrodent.

A

HYPOCHLORITE

21
Q

Caused by a high velocity fluid or gas striking the internal surfaces of a structure, in which the fluid or gas often contain solid particles.

A

IMPINGEMENT

22
Q

May be the result of impurities retained from the original extractive processes, the inclusions and imperfections introduced in casting and forming, or structure variations caused by heat treatment.

A

METTALURGICAL

23
Q

This form of corrosion may be encountered when it is made from ammonia.

A

NITRIC ACID HNO3

24
Q

It is a colorless, corrosive, toxic liquid that is an important industrial raw material that even attacks copper and high carbon 304 stainless steel.

A

NITRIC ACID HNO3

25
Q

Includes chemicals such as
ascetic acid CH3COOH
propionic acid CH3CH2COOH
formic acid HCOOH

A

ORGANIC ACID

26
Q

It is considered weak compared to others such as hydrochloric and sulfuric acid

A

ORGANIC ACID

27
Q

The gas that is considered the most corrosive.

A

OXYGEN O2

28
Q

It can be removed mechanically or chemically and is normally found in surface equipment

A

OXYGEN O2

29
Q

The use of plastic materials or internally plastic coating is a fairly common practice when this corrosion is expected. Cement lining is also effective.

A

OXYGEN O2

30
Q

Although not an actual form of corrosion, it can negatively affect production and transportation of products by restricting flow. It is affected by temperature, pressure and pH.

A

SCALE FORMATION

31
Q

Most carbonate, sulfate and iron compound scales can be prevented with scaling inhibitors and dissolved with acidic chemical solutions.

A

SCALE FORMATION

32
Q

Requires tensile stress, specific environmental conditions, and a specific set of mettalurgical factors.

A

STRESS CORROSION CRACKING SCC

33
Q

Increased levels of zinc in carbon steel alloys reduce this corrosion.
Well bonded coating will prevent this form of corrosion externally.

A

STRESS CORROSION CRACKING SCC

34
Q

Both low and high pH electrolytes are conducive to this corrosion.

A

STRESS CORROSION CRACKING SCC

35
Q

Cracking of a metal under the combined action of tensile stress and corrosion in the presence of water and hydrogen sulfide H2S.

A

SULFIDE STRESS CORROSION

36
Q

Dependent mainly on the temperature and chemical concentration of the corrodent.

A

SULFURIC ACID H2SO4

37
Q

It is only slightly corrosive at low temperatures and flow velocities.

A

SULFURIC ACID H2SO4

38
Q

Above 70% can be used with ordinary carbon steel.

Below 70% chemical lead is commonly utilized.

A

SULFURIC ACID H2SO4

39
Q

Results from stresses related to welding processes.

A

WELDMENT

40
Q

Accelerated by stress concentrations, material properties, fabrication, and weld size and quality.

A

WELDMENT

41
Q

Remedies include the use of proper weld procedures, correct cooling procedures (effective heat treatment), and proper technique.

A

WELDMENT