精馏塔理论塔板数计算VIP免费

ａ= 3判断点精-提线交点坐标R= 9TRUEx:0.19假定F= 100.00y:0.26D=29.353Xf=0.35Xd=0.955.8Xw=0.03q= -0.5Rmin= 1.672.4714R/Rmin=5.39X轴0.0000.0200.0300.1850.2200.255对角线y＝x0.0000.0200.0300.1850.2200.255平衡线方程y0.0000.0580.0850.4050.4580.507精馏段方程yn＋10.0950.113 0.1220.2620.293提馏段方程yn＋1-0.0150.0150.0300.2610.314q线方程xq0.0000.0200.0300.1850.2200.255q线方程yq0.2000.2070.2100.2620.2730.285塔板编号x:0.9410.8420.8420.6580.658y:0.9410.9410.8530.8530.687塔板编号x:0.4230.2320.2320.1420.142y:0.4760.4760.3320.3320.197塔板编号123456xi0.8640.6950.4620.2580.1640.091yi0.9500.8720.7200.511 0.3700.230说明:这里给出了最小Rmin算法,偏差比较大,可以调整R,达到精-提交点在平衡线上画图数据区1精折线提折线23芬斯克方程最少Nm＝精馏段塔板数：进料参数提馏段塔板数：123精馏塔逐板计算lelelbom解除密码：0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0 0.0 0.1 0.2 ]1)1([11minqDqDxxxxR0.2900.3250.3600.3950.4300.4650.5000.5350.5700.2900.3250.3600.3950.4300.0000.1850.5350.5700.5510.5910.6280.6620.6940.7230.7500.7750.7990.3250.3560.3880.4190.4510.4820.5140.5450.5770.3660.4180.4700.5230.5750.6270.6790.7310.7840.2900.3250.3600.3950.4300.0000.1850.5350.5700.2970.3080.3200.3320.3430.2000.2620.3780.3900.4230.4230.4230.4230.4230.4230.4230.4230.4230.6870.4760.4760.4760.4760.4760.4760.4760.4760.0760.0760.0350.0350.0130.0130.0010.001-0.0040.1970.0980.0980.0370.0370.0040.004-0.013-0.01378FALSEFALSEFALSEFALSEFALSEFALSEFALSE0.0440.0170.004-0.003-0.006-0.008-0.009-0.009-0.0090.1200.0500.011-0.009-0.019-0.024-0.027-0.028-0.028交点在平衡线上,回流比最小,记入Rmin计算理论塔34FALSEFALSEFALSEFALSE345FALSE 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0 对角线平衡线精馏段提馏段q线精折线提折线0.6050.6300.6750.7100.7450.7800.8150.8500.6050.6300.6750.7100.7450.7800.8150.8500.8210.8360.8620.8800.8980.9140.9300.9440.6080.6400.6620.7030.7340.7660.7970.8290.8360.8880.9250.9931.0451.0971.1491.2020.6050.6300.6750.7100.7450.7800.8150.8500.4020.4100.4250.4370.4480.4600.4720.4830.4230.4230.4230.4230.4230...