4.7 Article

Process analysis of improved process modifications for ammonia-based post-combustion CO2 capture

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ELSEVIER SCI LTD
DOI: 10.1016/j.jece.2020.104928

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Energy consumption; Heat integration; Absorption; Modeling and simulation

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Carbon-based fuels play a major role in global energy demand, but contribute to global warming. The need for cost-effective carbon sequestration schemes is emphasized due to increasing energy demand and climate change. Amine-based CO2 scrubbing is widely used for its high selectivity and pure CO2 production, although challenges in energy consumption and capture ratio exist. Investigating alternatives such as ammonia and developing new solvents, optimizing parameters, or process modifications can help reduce energy penalties.
Carbon-based fuels contribute majorly towards global energy demand; however, it results in global warming. The increasing energy demand and climate change highlights the need to develop cost-effective carbon sequestration schemes. Amine-based CO2 scrubbing have been widely used for their high selectivity and production of pure CO2. However, a challenge in implementing amine-based technology is high energy consumption with a low capture ratio. The energy penalty can be reduced either by introducing new solvents, optimizing parameters, or through process modifications. Recently, ammonia has tempted attraction in place of amines. In this present work, a Radfrac model in Aspen Plus is developed involving heat integration and absorption enhancement to overcome the barriers. The heat integration is performed with a rich solvent split and absorption enhancement is done with split flow arrangement. Further, the model is evaluated at different split ratios by performing heat integration between different streams of the flowsheet. Moreover, the process configurations used in this system is compared with MEA based process modifications concerning energy reduction. A competitive reduction in regeneration duty was observed which was 36% less than the reference NH3 and 47% less than the MEA process. This evaluated modification will result in maximum efficiency, a maximum level of CO2 capture, and a reduction in the reboiler duty. The rich solvent split and split flow process reduced the reboiler duty by 15.8% and 32.8%, respectively. The split flow process also indicated an increase of 17.2% in rich loading to recover 90% CO2.

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