Environmental statement - Flyndre and Cawdor - Maersk Oil
Environmental statement - Flyndre and Cawdor - Maersk Oil
Environmental statement - Flyndre and Cawdor - Maersk Oil
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<strong>Flyndre</strong> <strong>and</strong> <strong>Cawdor</strong> <strong>Environmental</strong> Statement<br />
Section 2 Proposed Development<br />
The Clyde platform will provide the necessary storage <strong>and</strong> injection equipment to enable the inhibitor<br />
to be injected at the wellhead/pipeline as required.<br />
2.7. CLYDE ‐ OVERVIEW OF EXISTING FACILITIES<br />
Talisman’s Clyde platform (Figure 2‐9) was commissioned in 1986 <strong>and</strong> is located approximately<br />
276xkm east southeast of Aberdeen <strong>and</strong> receives on‐platform production from the Clyde, Leven,<br />
Medwin <strong>and</strong> Nethan reservoirs (referred to as the Clyde fields) as well as production from the Orion<br />
reservoir via a subsea tie‐back. The platform also receives dry gas production from the Affleck<br />
reservoir, which is commingled with the export gas from the platform.<br />
Separate top side production facilities are dedicated to production of the Clyde field hydrocarbons<br />
<strong>and</strong> those of the Orion field hydrocarbons.<br />
2.7.1. CLYDE PRODUCTION PROCESS<br />
Figure 2‐9 Talisman’s Clyde platform.<br />
Reservoir fluids from the Clyde fields passes from the wellhead assembly via the high pressure<br />
manifold to a first stage separator or via the low pressure manifold to the second stage separator<br />
before entering the third stage separator (Clyde separators). The first <strong>and</strong> second stage separators<br />
are three‐phase (oil, water, gas) separators <strong>and</strong> the third stage is a two‐phase (gas, liquid) separator.<br />
A smaller test <strong>and</strong> clean‐up separator is provided to test wells individually without affecting<br />
production by operating in parallel with the first or second stage separator. The test separator has<br />
also been designed to serve as a back‐up to the first stage production separator when this is out of<br />
commission for cleaning or maintenance.<br />
Processed crude is drawn from the third stage separator through a crude oil dehydrator which<br />
removes the remainder of the water from the oil to a specification maximum of 0.2% basic sediment<br />
2‐ 16 D/4114/2011