乙醇—水相平衡线方程式

尊龙凯时乙醇-水溶液均衡数据乙醇-水溶液均衡数据（P=101.325kPa）液相构成气相构成沸面品量分数摩我分数品量分数摩我分数℃2.000.7919.708.7697.654.001.613尊龙凯时:乙醇—水相平衡线方程式(乙醇水的平衡相图方程)乙醇—水两相均衡相图t-x-y相图温度t/℃乙醇摩我分数乙醇摩我分数温度t/℃液相摩我分数x气相摩我分数y液相摩我分数x气相摩我分数y10099.999.899.799.599.29998.7597.6595

乙醇—水两相均衡相图t-x-y相图温度t/℃乙醇摩我分数乙醇摩我分数温度t/℃液相摩我分数x气相摩我分数y液相摩我分数x气相摩我分数y10099.999.899.799.599.29998.7597.6595

乙醇战水的尊龙凯时均衡相干图分享于610:52:10.0乙醇战水的均衡相干图文档格局xlsx文档页数:1页文档大小:12.23K文档热度:文档分类

乙醇水的平衡相图方程

乙醇-水两相均衡相图10.90.80.700图两：x-y相图11y0.60.50.40.30.20.1000.10.20.30.40.50.60.70.80.9x100.77880.42050.77880.000040.00040.00050.00120.00230.00

乙醇-水汽液均衡相图xY0.000040.00050.000120.00150.000160.0020.00020.00260.000240.00310.000270.00360.000310.00410.000350.00460.00040.00510.000550.00770

由相均衡圆程式按照乙醇—水整碎的相均衡数据可以查得(表一2.2.2最小回流等到操做回流比确切定当进料为饱战液体时则与2.3塔顶产物产量、釜残液量及减热蒸汽量的计

水-乙醇均衡相图00.0040.010.020.040.060.080.10.140.180.20.250.30.350.40.450.50.550.60.650.70.750.80.850.8940.90.95100.0530.110.1750.2730.340.3920.430.4820.5130.5

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