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The Use of Petroleum Coke as Fuel in a 10 kWth Chemical-Looping Combustor

Nicolas Berguerand (Institutionen för energi och miljö, Energiteknik) ; Anders Lyngfelt (Institutionen för energi och miljö, Energiteknik)
International Journal of Greenhouse Gas Control (1750-5836). Vol. 2 (2008), 2, p. 11.
[Artikel, refereegranskad vetenskaplig]

Tests were made in a 10 kWth chemical-looping combustor with a petroleum coke as the solid fuel and the oxygen carrier ilmenite, an iron titanium oxide. The fuel reactor is fluidized by steam and the oxygen carrier reacts with the volatiles released as well as the gasification intermediates CO and H2. A constant fuel flow corresponding to a thermal power of 5.8 kW was introduced into the fuel reactor and a total of 11 h of operation was reached. The effects of particle circulation and carbon stripper operation on solid fuel conversion, conversion of gas from the fuel reactor and CO2 capture were investigated. The actual CO2 capture ranged between 60% and 75% while the solid fuel conversion was in the range 66 to 78%. The low values of solid fuel conversion reflect loss of char due to low efficiency of the fuel reactor cyclone. The incomplete conversion of the gas from the fuel reactor is expressed as oxygen demand. The oxygen demand corresponds to the fraction of oxygen lacking to achieve full gas conversion and was typically 25%, due to presence of CH4, CO and H2 from the fuel reactor. Typical ratios of CH4, CO and H2 over the total gaseous carbon from the fuel reactor are respectively 5, 10 and 25%. Low loss of non-combustible fines from the system indicates very low attrition of the oxygen carrier.

Nyckelord: Chemical-Looping Combustion, Oxygen Carrier, Carbon Dioxide Capture, Interconnected Fluidized Beds, Solid Fuel Conversion

Denna post skapades 2008-01-14. Senast ändrad 2016-08-16.
CPL Pubid: 66008


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Institutioner (Chalmers)

Institutionen för energi och miljö, Energiteknik



Chalmers infrastruktur