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Surgil ESIA Report - Volume III - EKN

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“O’ZLITINEFTGAZ” PC<br />

PFS “<strong>Surgil</strong> field complex costruction with valuable<br />

components retrieval”<br />

According to results of hydraulic calculation, if the pipe diameter is 273х9mm and<br />

the collector maximum length is 3.8km, so the pressure loss makes 0.56MPa. Gas pressure<br />

and temperature at input in GS will make 7.24MPa and 39 0 С relatively.<br />

Gas collector<br />

Pressure – 10.78MPa<br />

Diameter – 273mm<br />

Length – 3.8km (each)<br />

At the given stage the anthropogenic impact will be expressed in use of the lands<br />

under construction of GGS and gas-field gathering mains, and also in emissions of gas<br />

combustion products in atmosphere on torches during purging of collectors sites (periodic<br />

and short-term).<br />

2.6 Complex Gas Treatment Unit (CGTU)<br />

For gas transportation through the main gas pipelines there are necessary careful<br />

clearing and dewatering of gas from solid impurities, aggressive components and moisture<br />

as they promote quick deterioration of the expensive equipment and cause disturbances in<br />

the conditions of normal operation.<br />

It is offered to carry out gas treatment on CGTU located on the field area, by method<br />

of low-temperature separations (LTS) with gas cooling at the expense of its expansion in<br />

turbo-expander.<br />

Treatment of the hydrocarbonic condensate allocated during gas separation on the<br />

LTS plant, is offered to make by open system of condensate gathering. Condensate is<br />

exposed to step aeration (separation, degassing) on the condensate separation and aeration<br />

plant. Gas condensate completely disappears under atmospheric pressure, and represents a<br />

stable condensate by saturated vapors pressure.<br />

Prevention of hydrate formation in the LTS plants is carried out by input of hydrate<br />

inhibitor into gas stream through sprayer directed towards gas flow for the best inhibitor<br />

dispersion in the gas stream and maintenance of its contact with water. It is offered to use<br />

diethyleneglycol (DEG) as anti-hydrate inhibitor on the CGTU.<br />

Production which is produced on the CGTU will be nonsulfurous dry combustible<br />

natural gas meeting on quality requirements of state standard Oz’DSt 948:1999 and stable<br />

gas condensate, meeting requirements of standard TSt 39.0-02:2004.<br />

CGTU productivity is defined proceeding from conditions of gas extraction from the<br />

field by years (including the term of attainment of constant extraction and the period of<br />

constant extraction) taking into account necessary requirements for reservation of<br />

equipment capacity.<br />

Design productivity of CGTU makes 3.0·10 9 m 3 per year. Productivity of one<br />

technological line of LTS for gas is 3.0·10 6 m 3 /day. Plant inlet pressure is 7.24MPa,<br />

<strong>Volume</strong> 2. Part 1. EIS Project for <strong>Surgil</strong> field construction<br />

45

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