Review
The calcium looping cycle for CO2 capture from power generation, cement manufacture and hydrogen production

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Abstract

Calcium looping is a CO2 capture scheme using solid CaO-based sorbents to remove CO2 from flue gases, e.g., from a power plant, producing a concentrated stream of CO2 (∼95%) suitable for storage. The scheme exploits the reversible gas–solid reaction between CO2 and CaO(s) to form CaCO3(s). Calcium looping has a number of advantages compared to closer-to-market capture schemes, including: the use of circulating fluidised bed reactors—a mature technology at large scale; sorbent derived from cheap, abundant and environmentally benign limestone and dolomite precursors; and the relatively small efficiency penalty that it imposes on the power/industrial process (i.e., estimated at 6–8 percentage points, compared to 9.5–12.5 from amine-based post-combustion capture). A further advantage is the synergy with cement manufacture, which potentially allows for decarbonisation of both cement manufacture and power production. In addition, a number of advanced applications offer the potential for significant cost reductions in the production of hydrogen from fossil fuels coupled with CO2 capture. The range of applications of calcium looping are discussed here, including the progress made towards demonstrating this technology as a viable post-combustion capture technology using small-pilot scale rigs, and the early progress towards a 2 MW scale demonstrator.

Research highlights

▶ A review paper on Ca-looping as a novel post-combustion CO2 capture scheme. ▶ Introduction to the technology including a review of current sorbent performance. ▶ The implications of integrating Ca-looping CO2 capture and cement production. ▶ Overview of results from world-wide Ca-looping pilot-plant scale trials. ▶ Advanced Ca-looping applications including H2 production/electricity generation.

Introduction

Carbon Capture and Storage (CCS) is a range of technologies being developed to help mitigate climate change by isolating from the atmosphere a significant fraction of the CO2 produced during fuel combustion (e.g., coal, gas and biomass). In the case of coal-fired power stations, the technology could prevent up to ∼90% of the CO2 from being emitted to the atmosphere; greater net emission reduction may be possible if coal is co-fired with biomass by accounting for the CO2 removed from the atmosphere during the biomass growth. CCS involves capture, purification and compression of the CO2 ready for transportation to a permanent storage location. This review focuses on CO2 capture, which is the most costly stage in the CCS process; for information on the topics of transport and storage please refer to Steeneveldt et al. (2006). The CO2 capture technology closest to market is post-combustion ‘scrubbing’ using amine-based solvents, which has been used for industrial-scale separation of CO2 for several decades. However, there are issues associated with amine-scrubbing for CO2 capture from a combustion flue-gas, including the high cost of manufacturing the solvent (e.g., MEA at ∼USD 1250/tonne) (Rao and Rubin, 2002), the high efficiency penalty (∼9.5–12.5 percentage points) (Xu et al., 2010), degradation of the solvent due to reactions with O2 and SO2 (frequently present in industrial flue gases), and the handling and disposal of large quantities of degradation products/waste solvent (which raises both environmental and health and safety concerns).

Research into a range of alternative CO2 capture technologies, which aim to address such issues, are being pursued all over the world and one promising technology involves the use of a solid CO2 sorbent using calcium-based materials, known as ‘The Calcium Looping Cycle’ or ‘Ca-looping’. This process offers a number of advantages, including; the use of well established fluidised bed technology; it is a high-temperature process and so high-grade excess heat can be recovered to provide additional energy to drive a steam cycle, thus reducing the overall efficiency penalty of the process; the materials used to perform the CO2 capture are widely available and environmentally benign (derived from limestones/dolomites); the affinity of the materials to SO2 provides simultaneous partial desulphurisation of the industrial flue gas; and, the waste material from the process has potential uses elsewhere in industry, most notably the cement industry. These advantages are discussed in detail herein.

Section snippets

Basics of the cycle

An extensive review of the Ca-looping cycle for CO2 capture has recently been published (Blamey et al., 2010); the main features of which are summarised herein. For further information, see also reviews by Stanmore and Gilot amongst others (Stanmore and Gilot, 2005, Harrison, 2008, Anthony, 2008, Florin and Harris, 2008a, Li and Fan, 2008), and the IEA GHG High Temperatures Solid Looping Cycles Network (IEA, 2010).

The Ca-looping process uses a CaO-based sorbent, typically derived from

The impact of Ca-looping on energy efficiency of power generation

As previously mentioned, key advantages of Ca-looping include the potential for retrofitting to existing power stations or other stationary industrial CO2 sources and the relatively low parasitic energy demand imposed on the existing processes. The Ca-looping cycle requires heat at the calciner to effect the following; the endothermic calcination of CaCO3; raising the temperature of the recycled sorbent from carbonator to calciner temperature (+250 °C); and, raising the temperature of fresh

Pilot plant trials for Ca-looping technologies

Several independent projects have been initiated in order to scale-up Ca-looping technology, including pilot plant trials with CO2 capture in the USA, Canada and Spain (up to ∼120 kWth) the details of which have been summarised above (Table 5). In addition, larger scale demonstrations are planned (∼2 MWth). To date, these projects have demonstrated good levels of CO2 capture efficiency (∼80–90%), with future work needing to focus on process efficiency and generating a CO2 stream suitable for

Advanced applications of Ca-looping technology—H2 production

Looking further into the future, Ca-looping technology underpins a range of advanced power schemes for the production of electricity and/or hydrogen coupled with the production of a concentrated stream of CO2 suitable for storage, or alternative industrial processes. These include: combined shift-carbonation (i.e., Han and Harrison, 1994) sorbent enhanced reforming (SER) (e.g., Balasubramanian et al., 1999, Johnsen et al., 2006), in situ CO2 capture, e.g., HyPr-RING (Lin et al., 2004a), Endex

Conclusions

The Ca-looping cycle has multiple potential benefits as a CO2 capture process for both post- and pre-combustion applications. It requires careful integration with the steam cycle of a power station if it is to be incorporated as a post-combustion CO2 capture process inexpensively. The degradation of the sorbent's ability to take up CO2 is manageable, though further work into both maintaining the overall reactivity of the sorbent and regenerating that reactivity, for multiple cycles of reaction,

Acknowledgements

The authors wish to thank the EPSRC for DTA studentships for Charles Dean and John Blamey, and the Grantham Institute at Imperial College for funding Dr Florin. The research leading to these results has received funding for Dr Al-Jeboori from the European Community's Seventh Framework Programme (FP7/2007–2013) under GA 241302-Caoling project.

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