A fluidized-bed combustion process with inherent CO2 separation; Application of chemical-looping combustion

By A. Lyngfelt, B. Leckner, T. Mattisson. 2001

975 citations recorded by the source corpus.

Subfields: Biomedical Engineering, Materials Chemistry, Renewable Energy, Sustainability and the Environment

View Paper: https://www.semanticscholar.org/paper/743cf5e5d4c8173e38b10f5690f208dcff15c66a

How researchers see this paper

The researchers whose trusted networks rank it highest, strongest advocate first. Every researcher gets a different order.

In Biomedical Engineering

1. T. Mattisson
2. A. Lyngfelt
3. M. Johansson
4. Mazen Abu-Khader
5. A. Abad
6. J. Adánez

In Materials Chemistry

1. A. Lyngfelt
2. T. Mattisson
3. M. Johansson
4. Mazen Abu-Khader
5. A. Abad
6. J. Adánez

In Renewable Energy, Sustainability and the Environment

1. A. Lyngfelt
2. T. Mattisson
3. Mazen Abu-Khader

Citations in the corpus

• Recent Progress in CO2 Capture/Sequestration: A Review (2006, background): “Chemical-looping combustion (CLC) with inherent separation of CO2 is considered a promising technology (Ishida and Jin, 1996, 1997; Ishida et al., 1998, 2002; Jin and Ishida, 2001, 2002; Jin et al., 1999; Lyngfelt et al., 2001).”
• Chemical-looping combustion of solid fuels – Status of development (2014, background): “The CLC system is composed of two interconnected fluidized bed reactors, an air and a fuel reactor, [1], Fig.”
• Investigation of Mn3O4 With Stabilized ZrO2 for Chemical-Looping Combustion (2006, background): “Chemical-looping combustion (CLC) is a combustion technology where an oxygen carrier is used to transfer oxygen from the combustion air to the fuel, thus avoiding direct contact between air and fuel (Anheden and Svedberg, 1998; Ishida et al., 1987; Lyngfelt et al., 2001).”
• Construction and 100 h of operational experience of a 10-kW chemical looping combustor (2005, background): “4 The reactors in Figure 1 could be designed in a variety of ways, but two interconnected fluidized beds have an advantage over alternative designs, because the process requires a good contact between gas and solids as well as a significant flow of solid material between the two reactors, [2].”