实验四：单釜与三釜串联返混性能测定
三釜实验数据处理表（釜一） T(s) 0 34 68 102 137 171 205 239 273 307 342 376 410 444 478 512 616 719 822 926 1029 1132 1236 1339 1442 1546 1649 1752 1857 1961 2064 计算基准： Σ t平均 方差σt 无因次方差σθ 模型参数N 22V1(mv) 1.507 10.395 9.032 7.895 6.939 6.104 5.418 4.821 4.312 3.893 3.519 3.197 2.963 2.717 2.556 2.361 2.001 1.807 1.657 1.578 1.536 1.503 1.484 1.473 1.465 1.453 1.453 1.454 1.445 1.444 1.445 1.507 L(ti) 0 8.888 7.525 6.388 5.432 4.597 3.911 3.314 2.805 2.386 2.012 1.69 1.456 1.21 1.049 0.854 0.494 0.3 0.15 0.071 0.029 -0.004 -0.023 -0.034 -0.042 -0.054 -0.054 -0.053 -0.062 -0.063 -0.062 L(ti)·△t 0 302.192 255.85 217.192 190.12 156.298 132.974 112.676 95.37 81.124 70.42 57.46 49.504 41.14 35.666 29.036 51.376 30.9 15.45 7.384 2.987 1935.119 ti·L(ti)·△ti 0 10274.528 17397.8 22153.584 26046.44 26726.958 27259.67 26929.564 26036.01 24905.068 24083.64 21604.96 20296.64 18266.16 17048.348 14866.432 31647.616 22217.1 12699.9 6837.584 3073.623 400371.625 ti·L(ti)·△ti 0 349333.952 1183050.4 2259665.568 3568362.28 4570309.818 5588232.35 6436165.796 7107830.73 7645855.876 8236604.88 8123464.96 8321622.4 8110175.04 8149110.344 7611613.184 19494931.46 15974094.9 10439317.8 6331602.784 3162758.067 142664102.6 2206.8976766 30917.03591 0.722248458 1.384565089