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

Citation
A. Lyngfelt et al., A fluidized-bed combustion process with inherent CO2 separation; application of chemical-looping combustion, CHEM ENG SC, 56(10), 2001, pp. 3101-3113
Citations number
27
Categorie Soggetti
Chemical Engineering
Journal title
CHEMICAL ENGINEERING SCIENCE
ISSN journal
00092509 → ACNP
Volume
56
Issue
10
Year of publication
2001
Pages
3101 - 3113
Database
ISI
SICI code
0009-2509(200105)56:10<3101:AFCPWI>2.0.ZU;2-V
Abstract
For combustion with CO2 capture, chemical-looping combustion has the advant age that no energy is lost for the separation of CO2. In chemical-looping c ombustion oxygen is transferred from the combustion air to the gaseous fuel by means of an oxygen carrier. The fuel and the combustion air are never m ixed, and the gases from the oxidation of the fuel, CO2 and H2O, leave the system as a separate stream. The H2O can easily be removed by condensation and pure CO2 is obtained without any loss of energy for separation. This ma kes chemical-looping combustion a most interesting alternative to other CO2 separation schemes, which have the drawback of a large energy consumption. A design of a boiler with chemical-looping combustion is proposed. The sys tem involves two interconnected fluidized beds, a high-velocity riser and a low-velocity bed. Metal oxide particles are used as oxygen carrier. The re activities needed for oxygen carriers to be suitable for such a process are estimated and compared to available experimental data for particles of Fe2 O3 and NiO. The data available on oxygen carriers, although limited, indica te that the process outlined should be feasible. (C) 2001 Elsevier Science Ltd. All rights reserved.