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• W2049002803 abstract "A thermally coupled multi-stage fluidized bed process was developed as a viable option for the carbon capture process with reduced energy consumption. The process is composed of multiple stages that operate at different temperature levels. Each stage consists of an absorber, a regenerator, and a heat exchanger for intra-stage heat recovery. Between adjacent stages, an absorber at a higher temperature stage is thermally integrated with a regenerator at a lower temperature stage to balance the supply and demand of thermal energy. A conceptual scheme of the process and an associated mathematical model was developed. Case studies of two- and three-stage fast fluidized bed processes are presented. For each stage, K2CO3, Na2CO3 promoted MgO, and Li4SiO4 are used as low-, medium-, and high-temperature solid sorbents which undergo independent gas-solid reaction pathways but with thermally coupled. The sorbents were chosen based on the availability of data on their kinetics and properties. A flow-sheet simulation of the developed process for a 500-MWe pulverized coal-based power plant was conducted using the Aspen Custom Modeler, to produce a process design study and a sensitivity analysis. Finally, the energy efficiency, including the net electrical efficiency, of the retrofitted power plant is compared with those of optimized MEA-based carbon capture processes and the calcium looping process." @default.
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• W2049002803 date "2014-07-01" @default.
• W2049002803 modified "2023-10-13" @default.
• W2049002803 title "A solid sorbent-based multi-stage fluidized bed process with inter-stage heat integration as an energy efficient carbon capture process" @default.
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• W2049002803 doi "https://doi.org/10.1016/j.ijggc.2014.03.012" @default.
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