串联反应釜停留时间分布的测定

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1、五、实验数据与处理1.根据所记录单釜、多釜实验中“结果显示”的数据表，用origin作出c(t)~t响应曲线；a)单釜实验数据表每组时间间隔：1.0S电机转速:200r/min主流体流量：20L/h数学期望:496.305328方差:186540.734375虚拟釜数:1.320457单釜停留时间分布b)多釜实验数据表每组时间间隔：1.0S电机转速:200r/min主流体流量：20L/h釜1数学期望:2046.543701釜1方差:-1604498.375000釜1虚拟釜数:-2.610374釜2数学

2、期望:399.457458釜2方差:113844.148438釜2虚拟釜数:1.401620釜3数学期望:489.181549釜3方差:84503.718750釜3虚拟釜数:2.8318116多釜停留时间分布1.采用离散化方法，，间隔取20~30组数据，求出单釜和多釜的以及模型参数N。a)单釜数据序号t/sc(t)/ms·cm-1t·c(t)/s·ms·cm-1t2·c(t)/s2·ms·cm-11600.81849.082944.821200.7488.81065631800.647116.4620

3、962.842400.591141.8434041.653000.523156.94707063600.464167.0460134.474200.454190.6880085.684800.384184.3288473.695400.323174.4294186.8106000.288172.8103680116600.247163.02107593.2127200.235169.2121824137800.218170.04132631.2148400.21176.4148176159000.17

4、1153.9138510169600.171164.16157593.61710200.152155.04158140.81810800.142153.36165628.81911400.127144.78165049.22012000.127152.41828802112600.118148.68187336.82213200.06991.08120225.62313800.115158.721900662414400.088126.72182476.82515000.091136.52047502

5、615600.079123.24192254.42716200.079127.98207327.62816800.096161.28270950.42917400.076132.24230097.63018000.069124.2223560∑7.9124375.34058248a)多釜釜1数据序号t/sc(t)/ms·cm-1t·c(t)/s·ms·cm-1t2·c(t)/s2·ms·cm-11601.49189.465367.621201.052126.2415148.831800.739133.

6、0223943.642400.517124.0829779.253000.356106.83204063600.24688.5631881.674200.18878.9633163.284800.13966.7232025.695400.10556.730618106000.07846.828080116600.06341.5827442.8127200.06647.5234214.4137800.03628.0821902.4148400.03126.0421873.6159000.02926.12

7、3490169600.01716.3215667.21710200.03939.7840575.61810800.02425.9227993.61911400.02427.3631190.42012000.01416.8201602112600.01417.6422226.42213200.01418.4824393.62313800.03953.8274271.662414400.01420.1629030.42515000.02436540002615600.03148.3675441.62716

8、200.01727.5444614.82816800.04168.88115718.4∑5.4481503.7966254.4a)多釜釜2数据序号t/sc(t)/ms·cm-1t·c(t)/s·ms·cm-1t2·c(t)/s2·ms·cm-11600.73744.222653.221201.011121.3214558.431801.006181.0832594.442400.928222.7253452.853000.823246.974070636