TOPIC 1: Gas Hydrates
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Figure 10 shows pipeline conditions
during normal operation, which is well
outside the gas hydrate stability zone. However, during shutdown when the
flow
rate is reduced, the pipeline temperature will drop to that of seawater
temperature, which could result in gas hydrate formation in the whole or some
sections of the pipeline. Hence, great care should be taken to avoid gas
hydrate problems during such operations.
Figure 10: Possible Pipeline Conditions –
Flowing and Shutdown
Conditions
To avoid gas hydrate problems during start-up and shutdown:
1. Analyse the hydrate phase boundary and the phase behaviour of the
system at normal operating and at shutdown conditions;
predictive
techniques could be used for this purpose, although some companies
may prefer experimental measurements.
2. After considering the minimum seawater temperature and the
maximum pressure (during shutdown and at initial start-up), inhibitor
could be injected whenever a shutdown is planned.
The amount of
inhibitor injected will depend on the amount of water in the system.
The injection of a thermodynamic inhibitor will shift the gas hydrate
phase boundary to the left.
3. In the case of start-up,
after an unplanned shutdown, it could be
necessary to inject inhibitor prior to start-up. The choice of inhibitor
depends on the condition of the pipeline, though generally methanol is
used due to its high vapour pressure.
4.
Alternatively, pipeline heating could be used if the necessary
infrastructure is in place.
TOPIC 1: Gas Hydrates
23
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ERIOT
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NIVERSITY B41OA December 2018 v3
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