Title of article :
Solar chemical reactor technology for industrial
production of lime
Author/Authors :
Anton Meier، نويسنده , , *، نويسنده , , Enrico Bonaldi، نويسنده , , Gian Mario Cella، نويسنده , , Wojciech Lipinski، نويسنده , , c، نويسنده , , Daniel Wuillemin، نويسنده ,
Issue Information :
ماهنامه با شماره پیاپی سال 2006
Abstract :
We developed the solar chemical reactor technology to effect the endothermic calcination reaction
CaCO3(s) !CaO(s) + CO2(g) at 1200–1400 K. The indirect heating 10 kWth multi-tube rotary kiln prototype processed
1–5 mm limestone particles, producing high purity lime that is not contaminated with combustion by-products.
The quality of the solar produced quicklime meets highest industrial standards in terms of reactivity (low, medium, and
high) and degree of calcination (exceeding 98%). The reactor s efficiency, defined as the enthalpy of the calcination reaction
at ambient temperature (3184 kJ kg 1) divided by the solar energy input, reached 30–35% for quicklime production
rates up to 4 kg h 1. The solar lime reactor prototype operated reliably for more than 100 h at solar flux inputs of about
2000 kW m 2, withstanding the thermal shocks that occur in solar high temperature applications. By substituting
concentrated solar energy for fossil fuels as the source of process heat, one can reduce by 20% the CO2 emissions in
a state-of-the-art lime plant and by 40% in a conventional cement plant. The cost of solar lime produced in a 20 MWth
industrial solar calcination plant is estimated in the range 131–158 $/t, i.e. about 2–3 times the current selling price of
conventional lime.
2005 Elsevier Ltd. All rights reserved.
Keywords :
Solar energy , Solar calcination , Solar lime , Rotary kiln , CO2 mitigation
Journal title :
Solar Energy
Journal title :
Solar Energy