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 kW(th) 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 U 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. (c) 2005 Elsevier Ltd. All rights reserved.