This paper was described about operation results of a 1t/d scale plant of Blue Tower Process which is two stages
pyrolyses, 1’st stage is pyrolysis at 550℃, and 2’nd stage is steam reforming at 950℃. Chopped road trees or Japanese cedar
chips and/or pellets were fed into the plant as raw materials. It was found that the gaseous low heating value was
approximately 11MJ/Nm3 and the concentration of hydrogen was ca. 45 volume %. The energy recovery efficiency on a ratio
of Output/Input was maximum 70.4%, and the comprehensive energy efficiency on a ratio of Output/Total input energy
which was Input energy + Utility energy was maximum 22.8%.
Next, tar was not observed at inner side of Pyrolyser and Reformer of the plant. It might be said that there would not be
few trouble on core components, i.e. Pyrolyser, Reformer and etc. of Blue Tower plant under on a practical use. Also, it was
generated a maximum power of 41 kW through the Blue Tower plant operation.
It was simulated about gas component from measured data of the plant, it was concluded that the both data were similar
in, so it was possible to be estimate gas components and energy efficiency of commercial plants precisely, by using the
simulated data based on the experiment.
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