Abstract
Natural gas processing plants (NGPP) contribute considerably to greenhouse-gas emissions, especially when processing carbon dioxide rich (CO2-rich) natural gas. Therefore, it is urgent and of general interest to study the decarbonization of such plants through new combined technologies and to estimate its economic–environmental performance through up-to-date metrics like the Marginal Abatement Cost (MAC). Comprehensive techno-economic and MAC analyses were conducted in the decarbonization of a NGPP through hybrid membrane permeation plus aqueous-monoethanolamine post-combustion capture. The NGPP processes 6.6 MMSm3/d of 44%mol CO2-rich gas. Hybrid decarbonization captured 94.05% of carbon dioxide abating carbon emissions from 2.69 t to 0.11 t per ton of treated gas, while power demand, investment, and manufacturing costs increased from 31.7 MW to 69.5 MW, 177.2 MMUSD to 325.4 MMUSD, and 238.8 MMUSD/y to 327.3 MMUSD/y, respectively. Simultaneously, revenues increased from 255.82 MMUSD/y to 421.78 MMUSD/y when 100% of carbon dioxide is utilized in enhanced oil recovery (EOR), leading to a 25-year net value increase from −1097 MMUSD to +441 MMUSD. For 80% carbon dioxide to EOR, the 25-year net value surpasses the counterpart of the carbon-emitting plant by 96.56 MMUSD with the same payback time (12 years). MAC decreased from 20.9 USD/tCO2 to −12.4 USD/tCO2 as carbon dioxide utilization changed from 0% EOR to 100% EOR. Since better net values and MACs were obtained for hybrid decarbonization with EOR, these retrofitted alternatives are more recommendable as they effectively reduce the carbon footprint by 54.53 MMtCO2 for 25 years of a profitable campaign.