论文部分内容阅读
研究了一定条件下气、液、固三相流化阳离子交换 -除 CO2 联合水处理装置的气含率分布 ,讨论了树脂层高及气、液表观速度对气含率分布的影响。用拟两相的双流体模型计算了三相流态化阳离子交换 -除 CO2 联合水处理装置的气含率。结果表明 ,模拟结果与实验结果一致
The gas holdup distribution of gas-liquid-solid three-phase fluidized cation-exchange (CO 2) combined water treatment unit under certain conditions was studied. The effect of resin height and gas and liquid superficial velocity on gas holdup distribution was discussed. The gas holdup of the three-phase fluidized cation exchange-carbon dioxide combined water treatment plant was calculated using a two-fluid two-fluid model. The results show that the simulation results are consistent with the experimental results