The experimental procedure is as follows Fuel, oil A.Which is similar, to diesel is burnt first for furnace heating. When.The temperature of primary and secondary air exceeds about.180 C primary air, is introduced into the mill to start mill heating.After a certain period woody biomass, is fed into the mill and theground biomass supplied to the burner. Mill exit temperature. And.Furnace exit gas temperature are monitored and controlled to stabilise.The operating condition. The stabilisation of mill is judged by.Mill differential pressure which is the pressure difference between.Upper part inside the mill and primary air chamber. It can be used.As an index which reflects the amount of circulating particles. If the.Feeding rate of fuel exceeds the mill capacity particles circulating,,Within the mill continuously increase which causes, the mill differential.Pressure, to increase too. After mill start-up the burner, is set.To co-firing fuel oil A and wood powder. Fuel oil A is cut off when.Woody biomass feeding reaches 1200 - 1500 kg / h and secondary air.Temperature exceeds 200 C. The wood powder is sampled and its.Particle size distribution analysed by sieve method (based on JIS.Z8815-1994).
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