附錄一物料平衡計算書

1.1-3-1.2-3-1.3-4-1.3.1物料衡-4-1.3.2加氫反應(yīng)工段物料衡-5-1.3.3乙二醇精制工段物-7--物料平衡計算書總99.9%301.1物料橫算式適用范類 物料衡算形 無化學(xué)反 有化學(xué)反 總項(xiàng)目核算物料衡算任333（8000）的連續(xù)操作，其中一年內(nèi)的四~五周（約30天）用于固定的停車設(shè)備檢修及緊急情況處理。物料衡算的主要加氫反應(yīng)工段物料衡圖1.1加氫反應(yīng)工段工藝路線圖表1.2加氫反應(yīng)工段總物料衡算To-C-PROD-TemperaturePressureVapor10101Enthalpy---TotalFlowTotalFlowTotalFlowMassFlow000000000000000000000TOTAL乙二醇精制工段物料衡算1.2乙二醇精制工段工藝路線圖1.3T1(脫甲醇塔)物料C-PROD-C-PROD-TemperaturePressureVapor0010Enthalpy----TotalFlowTotalFlowTotalFlowMassFlow4.576e-01.9144e-9.0089e-6.1596e-1.0465e-5.1045e-1.2287e-1.803e-0000Total1.4T2乙二醇一次精制物料衡算C-PROD-CC-TemperaturePressureVapor000Enthalpy---TotalFlowTotalFlowTotalFlowMassFlow002.0731e-3.5722e-6.2397e-2.028e-1.8556e-6.1596e-002.0731e-3.5722e-6.2397e-2.028e-1.8556e-00TOTAL1.5T3(萃取塔)物料衡C-TO-W1-TemperaturePressureVapor0000Enthalpy---TotalFlowTotalFlowTotalFlowMassFlow00004.9566e-0001.8842e-0002.7951e-0001.2206e-3.2348e-3.2356e-1.2205e-0TOTAL1.6T4萃取劑回收塔物料衡算W2-1-2TemperaturePressureVapor000Enthalpy--TotalFlowTotalFlowTotalFlowMassFlow0000000000003.9511e-3.2356e-3.2348e-7.6155e-TOTAL表1.7T5乙二醇二次精制塔物料衡算W1-D1-TemperaturePressureVapor000Enthalpy---TotalFlowTotalFlowTotalFlowMassFlow0000000000003.3846e-1.2205e-4.4423e-1.2205e-7.6614e-TOTALC-TemperaturePressureVapor000Enthalpy---TotalFlowTotalFlowTotalFlowMassFlow0003.5722e-2.028e-4.9566e-6.1596e-1.8842e-02.7951e-3.5722e-1.2206e-2.028e-00TOTAL1.9T7二酯原料回收塔物料衡算ETOH-DMO-TemperaturePressureVapor000Enthalpy---TotalFlowTotalFlowTotalFlowMassFlow0001.2201e-9.3873e-6.1596e-6.1595e-2.4265e-1.0398e-000TOTAL總1.10要原料消耗127.0972