Calcium and Chemical Looping Technology for Power Generation by Paul Fennell, Ben Anthony

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By Paul Fennell, Ben Anthony

Calcium and Chemical Looping know-how for energy iteration and Carbon Dioxide (CO2) Capture stories the elemental rules, platforms, oxygen companies, and carbon dioxide vendors proper to chemical looping and combustion.

Chapters assessment the marketplace improvement, economics, and deployment of those platforms, additionally delivering exact details at the number of fabrics and techniques that may support to form the way forward for CO2 capture prepared strength plants.

  • Reviews the elemental ideas, platforms, oxygen vendors, and carbon dioxide vendors correct to calcium and chemical looping
  • Provides a lucid clarification of complicated techniques and advancements in calcium and chemical looping, excessive strain structures, and replacement CO2 carriers
  • Presents details out there improvement, economics, and deployment of those systems

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Extra resources for Calcium and Chemical Looping Technology for Power Generation and Carbon Dioxide

Sample text

2 Main energy requirements in a calcium looping (CaL) system as a function of operating parameters. Adapted from Romeo et al. (2009). , 2008). Through a sensitivity analysis, the influence of parameters such as solid purge flow and solid circulation ratio on energy demand and cost of captured tonne of CO2 may be assessed, in order to obtain the operational window that yields an optimal scenario. 2. The solid circulation between reactors may be diminished without influencing the capture efficiency, by selecting fuels with a limited presence of inert material such as ashes and/or sulphur compounds, since these accumulate in the loop.

2012; Hossain & de Lasa, 2008). This topic is further discussed in Chapter 11. 3 CaL with CLC The chemical air separation carried out by means of a metallic oxide solid carrier in CLC may be applied to CaL. This combination allows the gaseous fuel to be oxidized in an N2-free environment, and for the removal of the ASU since the oxygen is provided in a different way. The concept requires three fluidized bed reactors, either a carbonator that may be fed by flue gas or a carbonator/gasifier fed by coal, an air reactor where oxygen is separated, and a calciner/fuel reactor where fuel is burned Energy and exergy pertaining to solid looping cycles 33 in the absence of nitrogen and limestone and the metallic oxide are regenerated (Abanades, Murillo, Fernandez, Grasa, & Martínez, 2010; Lisbona & Romeo, 2008; Manovic & Anthony, 2011).

Depending on the features of the global integration system, reduced costs of avoided CO2 have been found to be in the range of 18e23 $/ton CO2. , 2012). The avoided cost in a system with an oxyfired precalcination is been reported as 16 $/ton CO2 for adequate capture levels (around 90%). 2 Potential energy savings from CLC Depending on the fuel and the temperature level of the heat demands where surplus energy from CLC may be integrated, the selection of oxygen carriers should be chosen to optimize the efficiency of the fully integrated CLC system.

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