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Ca(OH)z during the latter part of gasification. Fixed carbon conversion at 850ยฐC without calcium is 65% after 2 h, whereas the catalysts achieve complete gasification within 1 h. The apparent activation energy is almost unchanged by calcium addition and the main product is Hz. Calcium increases Hz a
Ca(OH)z during the latter part of gasification. Fixed carbon conversion at 850ยฐC without calcium is 65% after 2 h, whereas the catalysts achieve complete gasification within 1 h. The apparent activation energy is almost unchanged by calcium addition and the main product is Hz. Calcium increases Hz a
Gaseous fuels ('derived gaseous fuels) preferred technology for this clean-up. A development programme on hot ga\ filtration has been carried out at CTDD in order to ensure that this component of the cycle can be used with minimum risk. Information has heen generated detailing the effect of filtrati
ities, property-estimation methods, dispersion modelling, and correction to the k-ยข model. Considerable differences were found in fuelvapour distribution when using different models, The LIF measurements and the numerical simulations were compared in terms of the fuel-vapour distribution. The simula
Solid fuels (derived solid fuels) set01 252 industry Research and development In the Australian coal Chham, R. L Energy Wor4 Dec. 1995. (234). i-xi. Over the last se.ven years the research infmatructure of Australia has gone 1995 Robens coal Science Lecture given by the author at The Royal Instituti