Feed-Gas to Netback Margin Screening

Compare a baseline and an alternative from raw sour feed gas through sweetening, NGL C2+ liquids recovery and sulphur, to sales-gas netback and operating margin.

Molecule-to-money flow Gas Production Intelligence

Baseline margin

$2.23B/yr

$6.11 per Mscf feed

Alternative margin

$2.26B/yr

$6.19 per Mscf feed

Uplift

+$31.1M/yr

Alternative vs baseline

Sales gas (alt.)

762 MMscfd

23.8% shrinkage · 1723 t/d sulphur

Revenue by product and processing cost

Annualised, both cases

Baseline case

Raw feed gas (MMscfd)H₂S in feed (mol %)CO₂ in feed (mol %)Fuel and flare (% of feed)NGL content (C2+) (bbl/MMscf)NGL recovery (%)Condensate yield (bbl/MMscf)Sales gas price ($/MMBtu)NGL price ($/bbl)Condensate price ($/bbl)Sulphur price ($/t)Sulphur recovery (%)Processing opex ($/Mscf feed)

Alternative case

Balance

Stream	Baseline	Alternative
Raw feed	1,000 MMscfd	1,000 MMscfd
Sales gas	774 MMscfd	762 MMscfd
NGL	52,800 bbl/d	57,000 bbl/d
Condensate	22,000 bbl/d	22,000 bbl/d
Sulphur	1,723 t/d	1,723 t/d
Margin	$6.1M/d	$6.2M/d

Screening balance only. Acid gas (H₂S + CO₂), fuel/flare and NGL shrink (2 Mscf/bbl) come off the feed; sales gas at 1.037 MMBtu/Mscf; sulphur from H₂S at 379.5 scf/lbmol. All inputs are DEMO assumptions you can edit.