The Calcium Looping (CaL) technology, based on the multicyclic carbonation/calcination of CaO in gassolid fluidized bed reactors at high temperature, has emerged in the last years as a potentially low cost technology for CO 2 capture. In this manuscript a critical review is made on the important roles of energy integration and sorbent behavior in the process efficiency. Firstly, the strategies proposed to reduce the energy demand by internal integration are discussed as well as process modifications aimed at optimizing the overall efficiency by means of external integration. The most important benefit of the high temperature CaL cycles is the possibility of using high temperature streams that could reduce significantly the energy penalty associated to CO 2 capture. The application of the CaL technology in precombustion capture systems and energy integration, and the coupling of the CaL technology with other industrial processes are also described. In particular, the CaL technology has a significant potential to be a feasible CO 2 capture system for cement plants. A precise knowledge of the multicyclic CO 2 capture behavior of the sorbent at the CaL conditions to be expected in practice is of great relevance in order to predict a realistic efficiency from process simulations. The second part of this manuscript will be devoted to this issue. Particular emphasis is put on the behavior of natural limestone and dolomite, which would be the only practical choices for the technology to meet its main goal of reducing CO 2 capture costs. Under CaL calcination conditions for CO 2 capture (necessarily implying high CO 2 concentration in the calciner), dolomite seems to be a better alternative to limestone as CaO precursor. The proposed techniques of recarbonation and thermal/mechanical pretreatment to reactivate the sorbent and accelerate calcination will be the final subjects of this review.
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