立式分离器计算

气体流量131181kg/h液体流量16262kg/h气体密度24.86kg/m3液体密度715.7kg/m3气体黏度液体黏度0.574CPLLLLTOLL1MINLLLTOHLL5MINHLLTOHHLL1MIN设定K0.09m/s设定值Vmax0.47m/s气体体积流量1.61235250710%裕量设备横截面积3.4m2设备直径D2190mm实际设备直径D2200mmH6=设备横截面积3.7994m2液体体积流量0.416566532m3/min10%裕量H1450mm设定LLLtoHLL550mmLLLLtoLL100mmHLLTOHHLL100mmH2750mm液体线速度Vl0.001827335m/sVt0.026237477合格，假设合理H3650设定H4450依据进口管嘴2200H5900设定H6150设定H7300设定容器总长3650mmT/T液体缓冲体积计算立式两相分离器计算，据GPSA计算H1=H2=H3=H4=H5=H7=𝑚3/s范围区间150100-150mm150mm300-900mm300-600mm3650450750650450900300