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Oil and gas production handbook - Process Control and ...

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Antifoam<br />

Polyelectrolyte<br />

Methanol (MEG)<br />

TEG<br />

separation in reasonable time. An emulsion breaker is added<br />

to prevent formation of, <strong>and</strong> break down of the emulsion<br />

layer by causing the droplets to merge <strong>and</strong> grow. S<strong>and</strong> <strong>and</strong><br />

particles will normally be carried out by the water <strong>and</strong> be<br />

extracted in water treatment. However, the emulsion can<br />

trap these particles <strong>and</strong> sink to the bottom as a viscous<br />

sludge that is difficult to remove during operation.<br />

The sloshing motion inside a separator will cause foaming.<br />

The foam will cover the fluid surface <strong>and</strong> prevent <strong>gas</strong> to<br />

escape. Also, the foam reduces the <strong>gas</strong> space inside the<br />

separator, <strong>and</strong> worst case it will pass the demister <strong>and</strong><br />

escape to the <strong>gas</strong> outlet as mist <strong>and</strong> liquid drops. An<br />

antifoam agent is introduced upstream of the separator to<br />

prevent or break down foam formation, by reducing liquid<br />

surface tension.<br />

Polyelectrolyte is added before the hydrocyclones <strong>and</strong><br />

causes oil droplets to merge. Works by reducing surface<br />

tension <strong>and</strong> water polarity. This is also called flocculation<br />

<strong>and</strong> polyelectrolyte flocculants <strong>and</strong> allows emissions to<br />

reach 40 ppm or less.<br />

Methanol or Mono Ethylene Glycol (MEG) is injected in<br />

flowlines to prevent Hydrate formation <strong>and</strong> prevent<br />

corrosion. Hydrates are crystalline compounds that form in<br />

water crystalline structures as a function of composition,<br />

temperature <strong>and</strong> pressure. Hydrates form <strong>and</strong> freeze to<br />

hydrate ice that may damage equipment <strong>and</strong> pipelines.<br />

For normal risers, hydrates form only when <strong>production</strong> stops<br />

<strong>and</strong> the temperature start to drop. Hydrate formation can be<br />

prevented by depressurization which adds to startup time or<br />

by Methanoli injection.<br />

On longer flowlines in cold seawater or arctic climates,<br />

hydrates may form under normal operating conditions <strong>and</strong><br />

require continuous methanol injection. In this case the<br />

methanol can be separated <strong>and</strong> recycled.<br />

Hydrate prediction model software can be used to determine<br />

when there is a risk for hydrate formation <strong>and</strong> to reduce<br />

methanol injection or delay depressurization.<br />

Tri Ethylene Glycol (TEG) is used to dry <strong>gas</strong>. See scrubbers<br />

<strong>and</strong> reboilers chapter.<br />

75

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