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化工原理精馏塔课程设计性能负荷图(已全编辑,输数即可)

2020-02-27 来源:乌哈旅游
严重漏夜线

组数

12346

howhwhLE设Lh(m3/h)

2.51.020.0049480.0445810.04952866101.0550.0128950.0445810.057476122181.060.0191720.0445810.063752696301.0650.0270770.0445810.07165818351.0750.030290.0445810.074870596

h系数

0.0015150.0015150.0015150.0015150.001515

u0M

7.5140177.8844798.1651848.5055678.640051

Vh(m3/h):3723.7673907.3594046.4694215.1554281.802操作弹性

液体流量下限线Lh(m3/h)Vh(m3/h)3.193650003.193611000液体流量上限线33取值 Lh(m/h)Vh(m/h)3.519.9250003.519.9211000组数12346过量雾沫夹带线设Lh(m3/h)how2.5101830350.0049480.0128950.0191720.0270770.03029hf0.1238220.143690.1593820.1791450.187176un(m/s)1.9431421.8247791.73131.6135621.565718溢流液泛线组数12345组数设Lh(m3/h)Lh/(lW)2.5E5101520253.7663877.53277411.2991615.0655518.8319411111how0.00770.0122230.0160160.0194030.022515hr(m)0.0001920680.0007682710.0017286090.0030730830.004801692hp(m)0.1948170.1897180.1849640.1802330.175393设充气系数he0.5629930.5602310.5581850.5566380.5555430.0291490.031540.0335430.0353350.036994气相动能因子Fa114597.322.2117782.673739214263.532.1612012.612598313955.582.1145412.556193Vh(m3/h)ua(m/s)4求取充气系数0.5629930.5629928860.5602310.5602308170.5581850.55818457213651.72.0684982.5005330.5566380.556637553513341.982.0215692.4438020.5555430.5555434316000h(m

3

/h):1.8831947.53277413.5589922.5983226.364712.9745461400012000100008000600040002000系列4下限线系列2系列3系列5上限线系列7Vh(m/h)An12824.3812043.211426.2610649.2110333.45

1.8332821.8332821.833282点1.8332821.833282

3001020304013.592998259.199

00

xy3.43927930003.4392793.439279

4200459054005700

7689876998751000011670120001270013500

上限线xy25.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.8769325.87693

3200398940004200490053005890679073008000879098881000014000120001300014000150003.6

干板压降hd(m)0.1656680.1581780.1514210.1448990.138399u0(m/s)29.4552728.7817128.1603227.5471526.922173.4392793.4392793.4392793.4392793.4392793.4392793.4392793.4392793.4392793.439279

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