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Circulating fluidized beds — diameter, solids hold-up, axial gas-mixing, and contact efficiency
- R. Contractor, R. Dry, C. White, Qi-Ming Mao, Stelios Konstantinidis, O. E. Potter
- 21 August 2000
Abstract Circulating fluidized beds (CFB) employed comprised: 0.0158 m riser diameter with 7.2 m height, 0.09 m riser diameter with 7.2 m height or 3.6 m height, and 0.254 m riser diameter with 10.5… Expand
Formation of NOx precursors during the pyrolysis of coal and biomass. Part VIII. Effects of pressure on the formation of NH3 and HCN during the pyrolysis and gasification of Victorian brown coal in…
Abstract Effects of pressure on the formation of HCN and NH 3 during the pyrolysis and gasification of Loy Yang brown coal in steam were investigated using a pressurised drop-tube/fixed-bed reactor.… Expand