气液相平衡实验数据处理

气甲苯% 0.486382 0.414289 0.34475 0.310223 0.305036 0.270993 0.269427
气环己烷% 0.513618 0.585711 0.65525 0.689777 0.694964 0.729007 0.730573
用非线性最小二乘法由平衡数据回归
选第一参数为0.912，第二参数为0.766
p1atm 1.209521 1.168241 1.105131 1.057208 1.032321 1.013957 0.98987
p2atm 0.499586 0.480202 0.450747 0.428535 0.417053 0.408606 0.397557
ห้องสมุดไป่ตู้
r1 1.149381 1.072005 1.089853 1.11582 1.052004 1.095358 0.996515
1.063382 1.058118 1.032024 1.139475 1.097798 1.071235 1.058909 1.043567 1.039912 1.021857 1.072354 1.051079 1.03735 1.030937 1.022919 1.021004 1.011514 1.027228 1.197402 1.133262 1.094504 1.077102 1.055986 1.051049
p2atm 0.499586 0.480202 0.450747 0.428535
y1计算 0.560437 0.646851 0.683738 0.689603
y2计算 0.321956 0.298902 0.269758 0.249465
A 0.000583 0.001541 6.79E-05 0.000372
0.7139 0.7466 0.7481 0.5363 0.6076 0.6755 0.7089 0.7139 0.7466 0.7481 0.5363 0.6076 0.6755 0.7089 0.7139 0.7466 0.7481 0.7481 0.5363 0.6076 0.6755 0.7089 0.7139 0.7466
0.2861 0.2534 0.2519 0.4637 0.3924 0.3245 0.2911 0.2861 0.2534 0.2519 0.4637 0.3924 0.3245 0.2911 0.2861 0.2534 0.2519 0.2519 0.4637 0.3924 0.3245 0.2911 0.2861 0.2534
填料塔停留时间分布实验数据处理 0.25 TD期望 DD方差 Ql升每时 QG方每时 UL Ped Rel 1.3 44.39 1819.18 200 1 0.008854 0.015 791.4897 1.83 28.99 569.16 200 2 0.008854 0.078 791.4897 1.74 27.58 450.1 200 3 0.008854 0.1098 791.4897 1.2 54.89 1823.19 100 1 0.004427 0.1044 395.7448 0.61 41.43 1193.1 150 1 0.006641 0.072 593.6173 0.48 42.55 1493.63 200 1 0.008854 0.0366 791.4897 0.76 35.83 1099.42 250 1 0.011068 0.0288 989.3621 0.01 34.33 928.63 300 1 0.013281 0.0456 1187.235 0.51 40.95 1674.9 350 1 0.015495 0.0006 1385.107 2.4 66.12 3598.56 100 2 0.004427 0.0306 395.7448 2.8 38.1 751.6 150 2 0.006641 0.144 593.6173 2.14 30.39 438.78 200 2 0.008854 0.168 791.4897 4.03 26.86 395.5 250 2 0.011068 0.1284 989.3621 1.91 21.29 170.09 300 2 0.013281 0.2418 1187.235 2.13 22.29 288.43 350 2 0.015495 0.1146 1385.107 2.67 49.71 1361.59 200 2 0.008854 0.1278 791.4897 2.27 38.21 712.6 200 2 0.008854 0.1602 791.4897 2.17 35.39 675.16 200 2 0.008854 0.1362 791.4897 2.1 33.28 603.4 200 2 0.008854 0.1302 791.4897 1.73 33.42 619.68 200 2 0.008854 0.126 791.4897 2.23 34.57 724.7 200 2 0.008854 0.1038 791.4897 2.05 32.85 580.33 200 2 0.008854 0.1338 791.4897 2.72 33.89 644.05 200 2 0.008854 0.123 791.4897 31.99 493.78 200 2 0.008854 0.1632 791.4897
0.342637 0.327779 0.241601 0.614228 0.514836 0.439154 0.399061 0.342637 0.327779 0.241601 0.614228 0.514836 0.439154 0.399061 0.342637 0.327779 0.241601 0.241601 0.614228 0.514836 0.439154 0.399061 0.342637 0.327779
第一参数 第二参数 x1 x2 y2 y1 lnr1 lnr2 r1 0.886 0.676 0.385772 0.614228 0.4637 0.5363 0.183246 0.048022 1.20111 0.886 0.676 0.485164 0.514836 0.3924 0.6076 0.132129 0.189815 1.141256 0.886 0.676 0.560846 0.439154 0.3245 0.6755 0.098164 0.309522 1.103143 0.886 0.676 0.600939 0.399061 0.2911 0.7089 0.081991 0.377588 1.085446
定液流量200
0.12 0.1
0.08 0.06 0.04 0.02 0 0 200 400 600 800 1000
二元气液平衡实验数据处理 A B C 查三参数Antoines有环己烷 6.84498 1203.526 219.482 甲苯 6.95464 1341.8 219.482 温度 液环己烷 液相甲苯 x1 x2 y2 y1 87.2 86 84.1 82.6 81.8 81.2 80.4 36.4452 46.2487 53.8331 57.8936 63.659 65.1872 74.1341 63.5548 53.7513 46.1669 42.1064 36.341 34.8128 25.8659 0.385772 0.485164 0.560846 0.600939 0.657363 0.672221 0.758399 0.614228 0.514836 0.439154 0.399061 0.342637 0.327779 0.241601 0.4637 0.3924 0.3245 0.2911 0.2861 0.2534 0.2519 0.5363 0.6076 0.6755 0.7089 0.7139 0.7466 0.7481
0.886 0.886 0.886 0.912 0.912 0.912 0.912 0.912 0.912 0.912 0.982 0.982 0.982 0.982 0.982 0.982 0.982 0.717 0.717 0.717 0.717 0.717 0.717 0.717
0.676 0.676 0.676 0.766 0.766 0.766 0.766 0.766 0.766 0.766 0.843 0.843 0.843 0.843 0.843 0.843 0.843 0.826 0.826 0.826 0.826 0.826 0.826 0.826
AA 目标函数 0.001288 0.110255 0.007709 0.015938 0.018888
1.615187 1.661205 1.978074 0.958557 1.09533 1.223126 1.301198 1.425819 1.4619 1.703759 0.881366 0.999 1.106251 1.170612 1.271656 1.300541 1.490208 1.622791 0.923864 1.056735 1.178861 1.252568 1.368883 1.402263
r2 1.511113 1.587217 1.639324 1.702224 2.00213 1.892002 2.622585
r2 p1atm 1.049194 1.209520696 1.209025 1.168241487 1.362774 1.105130955 1.458762 1.05720834
p1mmHg 919.2357 887.8635 839.8995 803.4783 784.5639 770.6074 752.3011
p2mmHg 379.6854705 364.9531986 342.5680515 325.686461 316.9605409 310.5404179 302.1435949
0.657363 0.672221 0.758399 0.385772 0.485164 0.560846 0.600939 0.657363 0.672221 0.758399 0.385772 0.485164 0.560846 0.600939 0.657363 0.672221 0.758399 0.758399 0.385772 0.485164 0.560846 0.600939 0.657363 0.672221
0.061455 0.056492 0.031522 0.130567 0.093307 0.068812 0.057239 0.042644 0.039136 0.021621 0.069856 0.049817 0.036669 0.030468 0.02266 0.020786 0.011449 0.026864 0.180154 0.1251 0.090301 0.074275 0.054475 0.049788
0.479451 0.507543 0.682124 -0.04233 0.091056 0.20141 0.263285 0.354747 0.379737 0.532837 -0.12628 -0.001 0.100977 0.157527 0.24032 0.262781 0.398916 0.484148 -0.07919 0.055184 0.164548 0.225195 0.313995 0.338087
1.032320871 1.01395709 0.989869828 1.209520696 1.168241487 1.105130955 1.05720834 1.032320871 1.01395709 0.989869828 1.209520696 1.168241487 1.105130955 1.05720834 1.032320871 1.01395709 0.989869828 1.209520696 1.168241487 1.105130955 1.05720834 1.032320871 1.01395709 0.989869828