Secondary Chemistry Flashcards

1
Q

Define GENERAL SG Degradation

A

Corrosion caused by the presence of Oxygen or Oxygen generating Contaminants

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2
Q

Define DENTING SG Degradation

A

Plastic deformation occurring at the tube support plates

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3
Q

Define WASTAGE SG Degradation

A

Localized corrosion caused by acidic attack in the low flow areas

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4
Q

Define PITTING SG Degradation

A

Localized attack at the sludge sites that may penetrate the S/G tube

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5
Q

Define STRESS CORRISION CRACKING SG Degradation

A

Tube cracking at the S/G U bend caused by chlorides and or stress

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6
Q

Define INTERGRANULAR ATTACK SG Degradation

A

Corrosion of S/G tube grain boundaries at tube sheet crevice or dry out areas

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7
Q

Define FRETTING SG Degradation

A

Local wear from impact or sliding of tubes against support plate or other tubes due to flow induced vibration

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8
Q

Define EROSION-CORROSION SG Degradation

A

Mechanical damage from impingement of SG tubes from suspended corrosion product or reactive chemicals

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9
Q

Define FATIGUE SG Degradation

A

Circumferential tube cracking as a result of cyclic flow or temperature stress

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10
Q

State the two functions provided by Hydrazine in reducing secondary plant corrosion

A

Scavenges Oxygen

Elevates pH

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11
Q

Explain why cation conductivity is a better indicator of condenser tube leakage than a standard conductivity measurement

A

taken after cations have been removed

Provides a very sensitive detection range due to lower “background”

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12
Q

State the specific locations sampled for cation conductivity on the High Range Conductivity Recorders located in the Control Room

A
Total Hotwell
Total Feedwater
SG Blowdown
Feedwater Cation 
Hotwell Cation
MUP Effluent
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13
Q

State the Chemistry parameters that are used to set the Limiting Conditions for S/G Operation as set forth by the chemical constituent administrative specifications.

A

Sodium
Chloride
Sulfate
Cation Conductivity

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14
Q

State the final maximum power permitted (long term) when conditions require entry into any of the three (3) action levels for high S/G contamination.

A

Action Level 1 - 21 days

Action Level 2 - Reduce power to 30 to < 50% within 24 hours

Action Level 3 - <5% power as quickly as safe plant operation permits

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15
Q

State one benefit gained from the following considerations when a power reduction is made in response to high S/G contamination: CONCENTRATION RATE

A

If from tube leak in condenser, it will reduce buildup in crevice areas, and will allow leak to be identified more easily from lower flow.

If the concentration rate is HIGH then extra measures may be required to prevent or minimize damage to the SGs. (increased blowdown)

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16
Q

State one benefit gained from the following considerations when a power reduction is made in response to high S/G contamination: RCS HOT LEG TEMPERATURE (T hot)

A

Intergranular & stress corrosion very temperature dependent.

Analysis has shown that “less damage” occurs at lower RCS Hot Leg temperatures than at elevated temperatures

17
Q

State one benefit gained from the following considerations when a power reduction is made in response to high S/G contamination: S/G HEAT FLUX

A

Reduced heat flux will reduce hard sludge formation.

As with RCS Hot Leg temps above, the lower the heat flux the less hideout/damage to the S/Gs.