回料流入口高度对循环流化床提升管流动特性的影响

The axial pressure drop profile and the radial solids distribution were measured in a circulating fluidized bed for evaluating the effects of return gas-solids stream position on the riser flow properties.The saturation carrying capacity of gas for Geldart B typed particles and the flow mode of return gas-solids stream in the bed were discussed.It was found that arranging the inlet at a higher position of the riser would make the bottom bed leaner when U0 was high and Gs was low.When Gs increased,the longer influenced region of return particles and a small air-staging through lifting the loosening air injection position made the bottom bed become denser significantly.The deceleration and residence of return particles caused a relatively denser but asymmetrical region in the vicinity of inlet.But much more symmetrical solids distribution profile was found in the upper and lower regions far away from the inlet.The effects of inlet height on the flow properties of the riser with air-staging also were analyzed.The secondary air injection below the solids inlet could not cut off the solids exchange in the bed.The bed solids concentration increased when the particles inlet moved to a higher position of the bed when air-staging was adopted.Using CO2 as tracer,the dispersion of the loop-seal-fluidizing air for transmitting the return particles was investigated.It was found that the loop-seal fluidizing air dispersion rate was low but can be enhanced by the secondary air injection.

大锥角锥形床内颗粒横向混合的实验研究

在900 mm×200 mm×800 mm的冷模试验台上,试验研究了带气体入口直段的大锥角锥形床内示踪颗粒的横向扩散过程,系统考察了床料粒径dp、过余速度u—u_(mff)、静止床层高度h和气体入口直段宽度δ对床内示踪颗粒横向扩散系数D_(sr)的影响。结果表明:在大锥角锥形床中,横向混合试验持续时间间隔对示踪颗粒横向扩散系数的计算结果影响较大;示踪颗粒的横向扩散系数D_(sr),随着床料粒径dp的增大而减小,随着过余速度u—u_(mff)静止床层高度h和气体入口段宽度δ的增大而增大。