实验数据处理

15.0030.0045.0060.0075.0090.003.504.004.505.005.506.006.507.007.508.008.509.000.25000.50000.75001.00001.50002.00002.50003.00003.50004.00004.50005.00005.50006.00006.50007.00007.50008.00008.50009.00000.25000.50000.75001.00001.25001.50001.75002.00002.25002.50002.75003.00003.50004.00004.50005.00005.50006.00006.50007.00007.50008.00008.50009.00000.150.611.411.932.613.814.815.776.347.067.437.7888.298.378.498.598.648.648.64

鼓风曝气

1.253.415.376.587.498.078.478.78.8999.099.149.169.219.259.269.169.179.189.29.179.179.179.17

9.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.170009.028.567.767.246.565.364.363.42.832.111.741.391.170.880.80.680.580.530.530.53

8.8376.6774.7173.5072.5972.0171.6171.3871.1971.0870.9970.9470.9270.8770.8370.8270.9270.9170.9070.8870.9170.9170.9170.917

105.00120.00135.00150.00165.00180.0010.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.08710.087射流曝气0.150.250000.610.500001.410.750001.931.000002.611.500003.812.000004.812.500005.773.000006.343.500007.064.000007.434.500007.785.0000085.500008.296.000008.376.500008.497.000008.597.500008.648.000008.648.500008.649.00000

沉淀数据up

00.000003.5799.320001.7688.290000.86535.500000.56915.130000.279

7.75000

50.68001011.71002064.50003084.87006092.2500

鼓风曝气

1.250.253.410.55.370.75

6.5817.491.258.071.58.471.75

8.728.89

2.2592.59.092.75

9.1439.163.59.2149.254.59.2659.165.59.1769.186.59.279.177.59.1789.178.59.17

9

120 100 80 p60 40 20 0 0加入活性炭的量

0.0020.0035.0050.0075.00100.001.55600.30800.03100.02900.01100.0110

3.570.680001.7611.710000.86564.500000.56984.870000.279

92.250000100.00000

活性炭吸附实验查标准溶液浓吸附量qe0.1571#DIV/0!0.03323.170000.0052.214290.00491.551000.00311.046000.00310.78450120 100 80 60 40 20 0 (20)010120.00000 100.00000 80.00000 p-160.00000 40.00000 20.00000 0.00000 03.502550.003171.6094380.0022142861.5892350.0015511.1314020.0010461.1314020.0007845

logqe

3.502550.5010592621.6094380.3452336581.5892350.1906117981.1314020.0195316851.131402-0.105407052

吸光度logcelogce臧红溶液标准曲线

0.16001.6020.08000.7590.04000.3550.02000.2010.01000.090.00500.030.0025

0.012

过滤实验

过滤过程t

4.00

1.000003.000005.0000010.0000020.0000030.00000

t

8.00

10.0000020.0000030.00000

1.81.6y = 10.03x -1.40.019R² = 0.9991.210.80.60.40.200.0000 0.0500 浊度

5.32.884.574.560.85度0.7

浊43210浊度

0.40.20.1

0 0.450.40.350.30.250.20.150.10.0505 冲洗强度膨胀率

9.000000.3512.000006.714.0000015.4916.0000018.31

20膨胀率（%）1510508 滤速

4.000006.000008.0000010.0000012.0000014.0000016.00000

水损

6111318192323

水损（cm)P-U关系曲线120120悬浮物去除率与沉速关系浊度12010080604020000.511.522.512010080604020000.511.5加FeSO40.070.060.050.040.030.020.0100y = 0.000x + 0.003R² = 0.989系线线v(ml)204060t(s)801001200.060.050.04v(ml)加Al2(SO4)3y = 0.000x + 0.001R² = 0.9650.030.020.01002040t(s)6080100DO

9.028.567.767.246.565.364.363.4t

0.250.50.7511.522.532.833.52.1141.744.51.3951.175.50.8860.86.50.6870.587.50.5380.538.50.53

9

0.258.8370.56.6770.754.71713.5071.252.5971.52.0171.751.61721.3872.251.1972.51.0872.750.99730.9473.50.92740.8774.50.83750.8275.50.92760.9176.50.90770.8877.50.91780.9178.5

0.9170.917

1086420024108n6t/mi420024DO/mDO0.250.500.751.001.522.533.544.555.566.577.588.59t0.150.611.411.932.61103.8194.8185.7776.3467.0657.437.784838.2928.3718.4908.590.00 8.648.648.64

2.00 4.00 6p-u关系曲线0.51u1.522.5悬浮物去除率与时间关系系列1对数(系列1)10203040506070悬浮物去除率与沉速关系曲线系列1对数(系列1)多项式(系列1)0.511.5u22.53ce

33.2

54.93.13.10.60.5logqe

0.501059260.345233660.19061180.01953168-0.1054071

y = 0.209x -0.1850.40.30.20.10f-0.10-0.20.511.522.533.50.1000 0.1500 0.2000 滤速为4m/h时浊度8765432100 5 10 15 20 t(min)25 30 35 滤速为8m/h时浊度滤速为8m/h时浊度10 15 20 t(min)25 30 35 冲洗强度与膨胀率关系曲线10 12 14 冲洗强度（L/（s.m2))16 18 滤速与清洁滤层水头损失曲线3025水损（cm)201510500 5 10 滤速（m/h)15 20 速关系曲线120悬浮物去除率与时间关系曲线1201008060402001.522.5-20020406080加FeCl30.090.080.07v(ml)y = 0.001x + 0.001R² = 0.999系列1线性(系列1)线性(系列1)0.060.050.040.030.020.01001020t(s)304050ty = -2.67ln(x) + 6.230R² = 0.983t对数(t)6810曝气鼓风DO-ty = 2.891x-0.71R² = 0.879曝气鼓风DO-t乘幂(曝气鼓风DO-t)6DO/mg/L8106.00 8.00 10.00 .5450