Abstract

Limestone (CaCO3) calcination to yield CaO plays a central role in a myriad of natural and industrial processes, among which the recently emerged Calcium Looping (CaL) process to capture CO2 is gaining a great relevance in the last few years. A main drawback of this process, however, is that calcination to regenerate the CaO sorbent particles must be necessarily carried out in short residence times and under high CO2 partial pressure in order to extract a highly concentrated CO2 stream from the calciner reactor. This requires raising up the calciner temperature, typically over 930 °C, which brings about an important energy penalty to the technology. Calcination can be speeded up by superheated steam through a chemical action involving H2O adsorption, but this catalytic effect leads also to excessively friable CaO solids. This poses an inconvenience for their transport in practice using circulating fluidized bed reactors, since the very fine particles that result from fracturing cannot be recovered by comm...

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