No abstract

The contribution of CO2 present in natural gas to the total GHG emissions of the gas plant can be significant (up to 20% for Middle East Gas). When both H2S and CO2 are present, the CO2 capture cost is currently very high. The method developed to tackle this challenge is an innovative architecture of the acid gas treatment chain based on a new ultra-selective absorption process. The redesigned acid gas treatment architecture is detailed and compared with available technologies on the market. The technical cost of avoided CO2 can be reduced by up to 70% by using the new ultra-selective process compared to the available CO2 capture technology. This new acid gas treatment architecture can reduce by up to 20% the energy consumption to capture CO2. A new ultra-selective solvent has been developed using computational screening tools combined with experiments measuring physical, operational, thermodynamic, and kinetic properties. Those serve as input of a process simulation tool validated with medium-pressure absorber and regenerator pilot plant data. The new solvent is currently at TRL4 validation, a selectivity of more than 75% (CO2 slippage) has been observed on the pilot plant, with a H2S specification in the treated gas kept around 5 ppm. This result is the consequence of both a new solvent formulation (selective amine) and optimal operating conditions. There is, moreover, no increase in regeneration duty for the new solvent.