Concept select · Small CO₂-rich sour gas · Indonesia

Acid Gas Route Screen

Enter a raw gas rate, CO₂ and H₂S content and the sales gas market. Compare six acid gas routes using the supplied screening basis. Explore the fuel demand, carbon intensity and gas value associated with each route.

Start with archetypes A to E, then adjust the feed and market. Inputs are saved only in this browser. Companion to the working paper Recover, Oxidize, or Inject? (IPA Convex 2027).

Feed gas

raw basis
MMSCFD
mol%
ppmv

Sales gas market

CO₂ spec
mol%

Paper archetypes

examples
Synthetic cases A to E from the paper Recover, Oxidize, or Inject? (IPA Convex 2027). They represent no specific field.
Basis and assumptions
°C
mol%
mg/Nm³
Permen LH 13/2009 Annex II item 2.b. An AMDAL can set a stricter value.
% raw gas
% of CO₂
Lowest CO₂ co-absorption assumed achievable when the market allows CO₂ slip.
ratio
Fraction of H₂S absorbed divided by fraction of CO₂ absorbed. Industrial 5 to 8, laboratory rotating packed bed about 40.
bar
USD/MMBTU
USD/t
%/yr
Example
Acid gas
H₂S in acid gas
Sulfur load
Oxidizer threshold

Route verdicts

Carried routes go to vendor quotes and study. Removed routes stop here.

RouteVerdictKey figureReason

Screening map

Hover or tab to a point for its values.

Acid gas H2S against sulfur load, with screening limits

Penalties

Value at concept select

Basis and limits

Equal co-removal of CO₂ and H₂S sets the base acid gas. The sales gas CO₂ specification bounds selective treating. The oxidizer is adiabatic, water-saturated acid gas at 25 °C, methane support fuel, no heat recovery, NIST Shomate enthalpies. SO₂ is reported dry at 25 °C, 1 atm and 0% O₂. Injection compresses from 1.6 to 80 bara in four stages and pumps to the set pressure, with a 33% gas-fired driver. Recovery routes vent the acid gas CO₂ and exclude utilities. Alkaline routes carry R/S, the CO₂ absorbed per mole of H₂S, with the selectivity S defined on absorbed fractions. Above 1 they are flagged conditional. The pH ceiling uses about 1.45 atm CO₂ and 0.18 to 0.71 M alkalinity. Carbon intensity divides the CO₂ emitted at the facility by the energy in the sales gas; the buyer's combustion adds about 53 kg per MMBTU (US EPA factor). Capital cost is out of scope.

This is a concept-select screen on public data. A carried route still needs vendor data, a permit check and, for injection, a subsurface assessment.

  1. Permen LH 13/2009, Annex II, items 2.a and 2.b. ppkl.menlhk.go.id
  2. US EPA AP-42 Section 8.13, Sulfur Recovery, 2015. epa.gov
  3. Merichem, LO-CAT process literature. digitalrefining.com
  4. SLB, THIOPAQ O&G product description. slb.com
  5. Mamrosh et al., Trimeric, short-contact-time caustic scrubbing; Schiavon Maia et al., Renewable Energy 109 (2017); Gupta et al., Appl. Microbiol. Biotechnol. 106 (2022). trimeric.com
  6. Sitawati et al., IPA13-BC-037, sales gas CO₂ specifications. ipa.or.id