Abstract: A new type of gas-liquid distributor with broken flow plate at the bottom of the distributor was designed. In the cold model experiment, crude oil and hydrogen was replaced by water and air. The experiment process is that water was pumped out from the water tank and flowed into the gas-liquid diffuser of the top of test tower after being measured by liquid flow meter. The gas-liquid flow were cooled by chilled box and flowed down through the distributor at the same time. The liquid entered the collecting device was guided into 17 numbered cylinders which were placed on the ground by rubber tubes. The left liquid entered the water tank. The gas was discharged into the atmosphere. Finally, the pressure drop was tested by U shaped tube differential pressure gauge. The distribute performance, pressure drop loss, operation flexibility of the vapor and liquid phases and distribution uniformity of the distributor was studied. The structural style parameters were also optimized and determined. Result showed the best technological conditions of the distributor were that the flow of liquid phase is 0.3m³/h, the flow of vapor phase is 20-30m³/h.

Key words: fixed-bed, fluid mechanics, reactors, gas-liquid flow

摘要： 设计了一种底部带有碎流板的新型管式气液分配器。以水和空气代替工业上的原油和氢气进行冷模实验。实验过程为:水由水箱经水泵抽出,经液体流量计计量后进入实验塔上部的气液扩散器,气液两相流经急冷箱冷却后同时向下通过分配器。进入到接液装置的液体通过橡胶管导入到放置在地面上的17个标有编号的量筒中,未进入接液装置的液体流入水箱,气体则排放到大气中。最后用U形管差压计测量分配器的压力降。实验研究了该分配器的分配性能、压力降损失、气液相操作弹性和分布不均度,优化并确定该分配器的结构形式和结构参数。结果表明,该分配器的最佳工作条件为:液相量为0.3m³/h左右,气相量为20~30m³/h。

关键词: 固定床, 流体力学, 反应器, 气液两相流