Situation
Analysis
SELECTING LOCATIONS
Choosing
monitoring locations based on convenience may not be indicative of what
is really happening. Proper equipment and location of monitoring sites
is critical for obtaining useful information and is ideally taken into
account during the design and fabrication stages. Most corrosion failures
occur at the lowest elevation in any system; the majority of failures
are at the bottom of pipes/vessels. Some corrosion occurs in risers or
in vessels/pipes with minimal flow and/or large temperature changes.
The severity
of corrosion attack is influenced by other local factors:
- Water
soluble components in the Gas phase (CO2, H2S)
-
Water soluble solids in the Liquid phase (carbonate, bicarbonate, chlorides,
sulphates)
-
Water soluble liquids in the Liquid phase (acids, alkalis, amines, glycols,
organic acids)
-
Insoluble solids which form sludges (clay, marine shells, sulphur elements,
amine products)
-
Living organisms such as algae and bacteria
Selecting
Monitoring Locations
Based
on historical data (past failures, visual inspections, UT or other
NDE information)
Based on system assessment to identify potential corrosion mechanisms
High temperature locations
Certain types of piping/vessel materials
System conditions (H2S, CO2, Amines)
Low spots in system – water or solid traps
Stagnant flow areas based on pipeline topography
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Specific
Considerations for Intrusive Monitoring Systems |
- Clearance
for retrieval equipment
- Pigging
requirements
- Inhibitor
injection
locations
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Monitoring
Interval Options
1 month interval |
active
system or monitoring new inhibitor programs |
3 - 4 month interval |
baseline
data or ongoing monitoring of active system |
6 month interval |
constant
process conditions - no significant activity |
Annual interval |
undesirable,
behind in information |
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