皂化反应测反应速度[汇总]

皂化反应测反应速度[汇总] [NaOH]=11.48 乙酸乙酯V=2mL 反应温度=29.8 ? BBBt/s PH LgC C LnC 1 10.88 -3.12 0.000758578 -7.1841 2 10.21 -3.79 0.000162181 -8.7267 3 9.41 -4.59 2.5704E-05 -10.568 4 8.91 -5.09 8.12831E-06 -11.720 5 8.53 -5.47 3.38844E-06 -12.595 6 8.27 -5.73 1.86209E-06 -13.193 7 8.12 -5.88 1.31826E-06 -13.539 8 8.04 -5.96 1.09648E-06 -13.723 9 7.99 -6.01 9.77237E-07 -13.838 10 7.95 -6.05 8.91251E-07 -13.930 11 7.91 -6.09 8.12831E-07 -14.022 12 7.88 -6.12 7.58578E-07 -14.091 13 7.85 -6.15 7.07946E-07 -14.160 14 7.82 -6.18 6.60693E-07 -14.229 15 7.8 -6.2 6.30957E-07 -14.276 16 7.79 -6.21 6.16595E-07 -14.299 17 7.77 -6.23 5.88844E-07 -14.345 气升式环流反应器流体力学及传质性能的测定实验数据 液体膨胀高度气量(m3/h) 清液层高度/mm 气含率ε /mm 0.5 950 965 0.0155 1 950 980 0.0306 1.5 950 990 0.0404 2 950 1010 0.0594 2.5 950 1020 0.0686 气量(m3/h) 循环距离L(m) 循环时间t(s) 液体循环速度uL(m/s) 0.5 2.36 5.7 0.4140 1 2.36 5.3 0.4452 1.5 2.36 5.1 0.4627 2 2.36 4.7 0.5021 2.5 2.36 4.3 0.5488 连续均相反应器提留时间分布的测定实验数据 t/s Cto Ct ?Ct Ft Et t*Et t*t*Et 0 0.773 0.408 0.408 0.0879 0.0879 0 0 10 0.743 0.378 0.786 0.1694 0.0814 0.8144 8.1447 20 0.71 0.345 1.131 0.2437 0.0743 1.4867 29.734 30 0.679 0.314 1.445 0.3113 0.0676 2.0297 60.892 40 0.654 0.289 1.734 0.3736 0.0622 2.4908 99.633 50 0.63 0.265 1.999 0.4307 0.0570 2.8549 142.74 60 0.607 0.242 2.241 0.4828 0.0521 3.1286 187.71 70 0.586 0.221 2.462 0.5305 0.0476 3.3333 233.33 80 0.567 0.202 2.664 0.5740 0.0435 3.4820 278.56 90 0.549 0.184 2.848 0.6136 0.0396 3.5681 321.13 100 0.533 0.168 3.016 0.6498 0.0361 3.6199 361.99 110 0.519 0.154 3.17 0.6830 0.0331 3.650 401.50 120 0.503 0.138 3.308 0.7127 0.0297 3.5681 428.18 130 0.492 0.127 3.435 0.7401 0.0273 3.5574 462.46 140 0.482 0.117 3.552 0.7653 0.0252 3.5294 494.11 150 0.472 0.107 3.659 0.7884 0.0230 3.4583 518.74 160 0.462 0.097 3.756 0.8093 0.0209 3.3441 535.05 170 0.453 0.088 3.844 0.8282 0.0189 3.2234 547.98 180 0.446 0.081 3.925 0.8457 0.0174 3.1415 565.48 190 0.439 0.074 3.999 0.8616 0.0159 3.0295 575.60 200 0.426 0.061 4.06 0.8748 0.0131 2.6287 525.74 210 0.421 0.056 4.116 0.8868 0.0120 2.5339 532.12 220 0.417 0.052 4.168 0.8980 0.0112 2.4649 542.29 230 0.412 0.047 4.215 0.9082 0.0101 2.3292 535.72 240 0.408 0.043 4.258 0.9174 0.0092 2.2236 533.67 250 0.404 0.039 4.297 0.9258 0.0084 2.1008 525.21 260 0.401 0.036 4.333 0.9336 0.0077 2.0168 524.36 270 0.398 0.033 4.366 0.9407 0.0071 1.9198 518.35 280 0.392 0.027 4.393 0.9465 0.0058 1.6289 456.10 290 0.389 0.024 4.417 0.9517 0.0051 1.4996 434.90 300 0.387 0.022 4.439 0.9568 0.0047 1.4221 426.63 310 0.385 0.02 4.459 0.9607 0.0043 1.3359 414.13 320 0.384 0.019 4.478 0.9648 0.0040 1.3100 419.21 330 0.382 0.017 4.495 0.9685 0.0036 1.2087 398.90 340 0.381 0.016 4.511 0.9719 0.0034 1.1721 398.53 350 0.379 0.014 4.525 0.9750 0.0030 1.0558 369.53 360 0.378 0.013 4.538 0.9774 0.0028 1.0084 363.02 370 0.376 0.011 4.549 0.9801 0.0023 0.8769 324.47 380 0.375 0.01 4.559 0.9823 0.0021 0.8187 311.13 410 0.373 0.008 4.584 0.9877 0.0017 0.7067 289.76 420 0.372 0.007 4.591 0.9892 0.0015 0.6334 266.06 430 0.371 0.006 4.597 0.9905 0.0012 0.5559 239.04 440 0.371 0.006 4.603 0.9918 0.0012 0.5688 250.29 450 0.37 0.005 4.608 0.9928 0.0010 0.4848 218.16 460 0.369 0.004 4.612 0.9937 0.0008 0.3964 182.37 470 0.369 0.004 4.616 0.9946 0.0008 0.4050 190.39 480 0.368 0.003 4.619 0.9952 0.0006 0.3102 148.93 490 0.368 0.003 4.622 0.9959 0.0006 0.3167 155.20 500 0.368 0.003 4.625 0.9967 0.0006 0.3232 161.60 510 0.368 0.003 4.628 0.9971 0.0006 0.3296 168.13 520 0.367 0.002 4.63 0.9976 0.0004 0.2240 116.52 530 0.367 0.002 4.632 0.9983 0.0004 0.2283 121.05 540 0.367 0.002 4.634 0.9984 0.0004 0.2327 125.66 550 0.367 0.002 4.636 0.9989 0.0004 0.2370 130.35 560 0.367 0.002 4.638 0.9993 0.0004 0.2413 135.14 570 0.367 0.002 4.64 0.9997 0.0004 0.2456 140.01 580 0.366 0.001 4.641 1 0.0002 0.1249 72.484 求和 1 96.877 18489 , tE(t),,96.8770平均停留时间t , ==96.877 ,1E(t),0 ,2t,E(t),184982220,,,t,,96.877,9112.85方差t,1E(t) ,0 2,9112.852t,,,0.971,22t96.877 11 模拟级数N,,,12,0.971 稳态法气相扩散系数的测定实验数据 O丙酮-空气体系 体系温度=45 液面初始高度Z0=27.88 cmC 大气压=1 atm 累计时间t 测高仪读数Zi序号 换算成(cm) min y y/2 t/y s 1 0 0 27.88 2 15 900 27.42 0.46 0.23 1956.52 3 30 1800 26.94 0.48 0.24 3750 4 45 2700 26.37 0.57 0.285 4736.845 5 60 3600 25.6 0.77 0.385 4675.32 -5 C,3.8，10 P,PAORT,2A D,Cln(),0.7589cm/sAB0PP,PA 液固体系的无机陶瓷膜分离实验数据 循环流量 操作压强p/渗透通量渗透通量操作压差?循环流量(m3/h) (Mpa) J(ml/10s) J(m3/h) p/(Mpa) (L/h) 3.8 0.05 25 90000 3800 4.3 0.06 45 162000 0.01 4300 4.8 0.07 60 216000 0.02 4800 5.3 0.085 84 302400 0.035 5300 5.8 0.1 100 360000 0.05 5800 6.3 0.11 125 450000 0.06 6300 6.8 0.122 150 540000 0.072 6800 7.3 0.14 175 630000 0.09 7300 7.7 0.15 195 702000 0.1 7700