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Surgil ESIA Report - Volume III - EKN

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<strong>Surgil</strong> <strong>ESIA</strong> <strong>Report</strong> - <strong>Volume</strong> <strong>III</strong><br />

Figure A.12: GSP Process Schematic<br />

Source: Technical Review <strong>Report</strong>, Nexant, Feb 2011<br />

A.3.2.1. Reception Facilities<br />

The volume of the combined feed gas from <strong>Surgil</strong> and East Berdakh Fields will be measured with a new<br />

inlet gas metering station. Downstream of the metering station, there will be a feed gas inlet filter<br />

separator, where entrained hydrocarbon liquids are separated from the feed gas and are routed to the<br />

Unstabilized Condensate Treatment Plant. The gas will then be re-compressed with a feed gas<br />

compressor and sent to Feed Gas Chilling, Dehydration & Mercury Removal Unit.<br />

A.3.2.2. Feed Gas Chilling, Dehydration and Mercury Removal Unit<br />

Molecular sieve technologies will be used for the dehydration and mercury removal process steps.<br />

Molecular sieves are adsorbents composed of aluminosilicate crystalline polymers (zeolites) which<br />

efficiently remove low concentrations of polar or polarisable contaminants such as water, methanol,<br />

hydrogen sulphide, carbon dioxide, COS, mercaptans, sulfides, ammonia, aromatics and mercury down to<br />

trace concentrations. Molecular sieves will also reduce water concentration to less than 1ppm which is<br />

necessary for further downstream processing.<br />

Mercury is typically removed to prevent risk of metal embitterment of downstream plant. The exact process<br />

design is not fully confirmed at this point and may include the mercury removal facility being placed after<br />

the dehydration unit, or combined with the dehydration unit.<br />

254793/RGE/GEV/03/01/03/08/2011<br />

11

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