Andrew Infrastructure Specific Information
Entry Spec
Exit Spec
Topsides Design:
H2S 10 ppm, CO2 2.25 mol-% (dry basis)

Have a hydrocarbon dewpoint which all the pressures in excess of ten
thousand three hundred and forty (10340) KPa gauge does not exceed
minus two (-2) Deg C.

Have a maximum water content to be the lesser of: (1) fifteen (15) KG per
million cubic metres or (2) that content equivalent to a water dewpoint at
seven thousand five hundred (7500) KPa gauge of minus twenty (-20)
deg C.

Have a maximum hydrogen sulphide content to be three decimal point
three (3.3) ppmv.

Have a maximum sulphur content to be fifteen decimal point zero (15.0)
ppmv measured as hydrogen sulphide.

Have a maximum carbon dioxide content to be three decimal point zero
(3.0) mol %.

Have a maximum oxygen content to be ten decimal point zero (10.0)
ppmv.

Have a maximum total non-hydrocarbon content to be five decimal point
five (5.5) mol %.

Have a maximum delivery pressure at the delivery point of seventeen
thousand two hundred and thirty (17230) KPa gauge.

Have a maximum temperature at the delivery point of fifty one (51) deg C.
Details of Primary separation
processing facilities
Andrew has a single process train with 2 stages of separation & another primary
single stage of LP separation that ties-in the LP stage of main train
Details of Gas treatment facilities
Andrew has a single gas processing train with gas dehydration facilities; includes
LP, 2-stage HP and re-injection compressor