Effects of riser height and total solids inventory on the gas–solids in an ultra-tall CFB riser

More and more CFB boilers with large capacity and ultra-tall furnaces are used for power generation. Understanding the fluid dynamics in the ultra-tall furnace is important. However, existing studies on fluid dynamics in the CFB furnace are limited to the risers with rather short height. An experimental study was conducted with a cold CFB test rig of 240 mm in I.D. and 38 m and 54 m in height respectively. The influences of total solid inventory Iv, and fluidizing gas velocity Ug on the axial voidage profile along the riser and solid circulation rate Gs were investigated. Experimental results showed that when Ug exceeded the transport velocity, an S-shaped voidage profile characterized by fast fluidization was established in the riser. In such circumstance, the voidage at top dilute section kept constant and Gs reached saturation carrying capacity (Gs = Gs⁎) and inappreciably change with riser height and Iv. Moreover, Gs⁎ increased from 40 kg to 50 kg when the riser height increased from 38 m to 54 m. The results indicated that even for the 600 MWe supercritical CFB boiler with a 54 m tall furnace, only a modest increase of Iv and power of forced draft fans is needed to obtain high enough Gs to meet the requirements of heating surfaces arrangement in furnace and the circulation loop. The necessary conditions to form the S-shaped profile of voidage in the riser were also discussed.

The influences of total solids inventory Iv, and fluidizing gas velocity Ug on the axial voidage profile along the riser and solids circulation rate Gs are investigated in a cold CFB test rig of 240 mm in I.D. and 38 m and 54 m in height respectively. The critical total solids inventory for saturation carrying capacity was found to increase from 40 kg to 50 kg when the riser height increased from 38 m to 54 m.Figure optionsDownload as PowerPoint slide