气相法PE装置脱挥单元的数值模拟及应用

摘要

基于费克扩散定理、亨利定律、质量守恒定律等，结合气相法工艺聚乙烯（PE）装置脱挥单元中脱气仓的运行情况，建立了脱气仓的数学模型。运用该模型定量分析了N2流量、停留时间、压力等操作条件对脱气仓操作曲线和脱挥性能的影响，模拟分析了300kt/a气相法PE装置脱挥单元，确定了优选操作条件：操作点应同时位于出口处组分的质量分数与N2流量关系曲线的转折点，以及N2流量与停留时间关系曲线的转折点附近；N2流量与PE流量之比为0.010~0.040。%The resin degassing unit mathematical model of gas-phase fluidized bed polyethylene process was established based on Fick's diffusion law, Henry's law, mass conservation equation and so on. Then the model was applied to quantitatively analyzing the impact of the operating conditions such as nitrogen flow rate, residence time and pressure on the operation curve of purge bin and degassing performance curve, and simulation analysis of resin degassing unit in a 300 kt/a gas-phase polyethylene installations was performed to determine the preferred operating conditions. Specific conditions: operating point should be located at the turning point on outlet mass percentage of the components-nitrogen flow curve and at the turning point on nitrogen flow-residence time curve, and the flow ratio of nitrogen to polyethylene ranged from 0.010 to 0.040.