(628g) Automated Process Design and Techno-Economic Assessment of Membrane-Based CO2 Capture Systems
AIChE Annual Meeting
2018
2018 AIChE Annual Meeting
Separations Division
Membranes for CO2 Capture
Thursday, November 1, 2018 - 10:06am to 10:27am
Considerable efforts from academic and industrial communities have been made to develop cost-effective and energy-efficient CO2 capture processes. A wide range of separation techniques, for example, amine solvents, dry sorbent and membranes, are available, and Techno-Economic Assessment (TEA) is necessary to evaluate technical feasibility and compare economics in a systematic and fair manner. In this presentation, Techno-Economic Assessment model will be addressed, with which economic evaluation of membrane-based CO2 capture processes is made and then comparison is made with other capture technologies, for example, amine-based capture process, for gaining conceptual insights in the development required for membrane process in the context of CO2 capture. Based on TEA model presented, CAPEX and OPEX of membrane-based CO2 capture process is obtained, subject to economic parameters and process design constraints. CO2 capture cost and avoidance cost are also estimated. TEA also accommodates economic benefits gained from the application of process integration between CO2 emitting plant and CO2 capture process, while process optimization technique is fully used for minimizing overall cost at the capture process level. Sensitivity analysis is made to understand techno-economic impact of process design and their performance on capture cost. The membrane-based CO2 separation process is simulated and optimized with authorsâ in-house process design framework developed in MATLAB® environment, which can effectively identify the cost-effective configuration of multi-stage membrane systems, together with full consideration of CO2 liquefaction. Case study will be given to demonstrate the benefits of TEA for critical and systematic evaluation of different capture technologies in a holistic manner.
Acknowledgement
This research was supported by the Korea Carbon Capture & Sequestration R&D Center (KCRC) through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, and ICT (NRF-2014M1A8A1049338)