perhitungan pompa

27
996.59 9.8 No Variasi BPsuction Pdischarge (kgf/cm2) 1 46.67 0 0.25 24516.625 2 26.67 0 0.33 32361.945 10 20 0 0.37 36284.605 3 16.67 0 0.45 44129.925 4 13.33 0 0.5 49033.25 5 10 0 0.7 68646.55 6 8.33 0 0.75 73549.875 7 6.67 0 1.04 101989.16 8 5 0 1.33 130428.445 9 1.667 0 2 196133 No Variasi BPsuction Pdischarge (kgf/cm2) 1 46.67 0 0.25 24516.625 2 26.67 0 0.33 32361.945 10 20 0 0.38 37265.27 3 16.67 0 0.43 42168.595 4 13.33 0 0.5 49033.25 5 10 0 0.63 61781.895 6 8.33 0 1 98066.5 7 6.67 0 1.22 119641.13 8 5 0 1.82 178481.03 9 1.667 0 2.2 215746.3 piknometepikno kospikno isivol fluida 1 15 25.6 10.63626968 2 15 25.6 10.63626968 T ruang 26 rho air 0.9968 25 0.99708 data geankoplis 30 0.99568

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996.599.8 gravitasi 9.8

No Variasi Bu Psuction ( Pdischarge (kgf/cm2) V(x10 t flow1 46.67 0 0.25 24516.625 0.005 12.762 26.67 0 0.33 32361.945 0.005 13.164

10 20 0 0.37 36284.605 0.005 13.3483 16.67 0 0.45 44129.925 0.005 13.6664 13.33 0 0.5 49033.25 0.005 14.137

5 10 0 0.7 68646.55 0.005 15.4846 8.33 0 0.75 73549.875 0.005 16.2117 6.67 0 1.04 101989.16 0.005 19.0568 5 0 1.33 130428.445 0.005 24.1299 1.667 0 2 196133 0.005 50.123

No Variasi Bu Psuction ( Pdischarge (kgf/cm2) V(x10 t flow1 46.67 0 0.25 24516.625 0.005 10.1292 26.67 0 0.33 32361.945 0.005 13.131

10 20 0 0.38 37265.27 0.005 13.294

3 16.67 0 0.43 42168.595 0.005 13.487

4 13.33 0 0.5 49033.25 0.005 13.8555 10 0 0.63 61781.895 0.005 15.1936 8.33 0 1 98066.5 0.005 18.6557 6.67 0 1.22 119641.13 0.005 22.6798 5 0 1.82 178481.03 0.005 41.1499 1.667 0 2.2 215746.3 0.005 64.298

piknomete pikno koso pikno isi vol fluida vol pikno rho fluida1 15 25.6 10.63626968 10.63403 0.996802 15 25.6 10.63626968 10.63403 0.9968

T ruang 26

rho air 0.9968

25 0.99708 data geankoplis30 0.99568

m/s

t daya delta P Q (laju alir) h (head pump) p listrik p hidrolik efisiensi14.385 24516.63 3.92 2.51 200.21 9.61 4.80 14.172 32361.95 3.80 3.31 203.22 12.29 6.05 14.097 36284.60 3.75 3.72 204.30 13.59 6.65 14.057 44129.93 3.66 4.52 204.88 16.15 7.88

13.82 49033.25 3.54 5.02 208.39 17.34 8.32

13.382 68646.55 3.23 7.03 215.21 22.17 10.30 13.352 73549.88 3.08 7.53 215.70 22.69 10.52 12.929 101989.16 2.62 10.44 222.76 26.76 12.01 12.113 130428.45 2.07 13.35 237.76 27.03 11.37 10.622 196133.00 1.00 20.08 271.14 19.57 7.22

t daya delta P Q (laju alir) h (head pump) p listrik p hidrolik efisiensi15.475 24516.63 4.94 2.51 186.11 12.10 6.5015.353 32361.95 3.81 3.31 187.59 12.32 6.5715.156 37265.27 3.76 3.82 190.02 14.02 7.38

15.064 42168.60 3.71 4.32 191.18 15.63 8.18

14.943 49033.25 3.61 5.02 192.73 17.70 9.1814.823 61781.90 3.29 6.33 194.29 20.33 10.4613.795 98066.50 2.68 10.04 208.77 26.28 12.5913.075 119641.13 2.20 12.25 220.27 26.38 11.9811.504 178481.03 1.22 18.27 250.35 21.69 8.6610.915 215746.30 0.78 22.09 263.86 16.78 6.36

0

Head run 1

1,549,516

d t

50.19 49.47 0.72 0.5184 0.528541 2.93168643.92 42.51 1.41 1.988141.83 40.97 0.86 0.739637.65 37.18 0.47 0.220933.46 32.78 0.68 0.462432.42 31.75 0.67 0.448920.91 21.51 -0.6 0.3618.82 18.64 0.18 0.032417.78 17.61 0.17 0.028916.73 16.39 0.34 0.1156

d total 4.9 4.9152

d rata-rata 0.49 0.49152

n 10 0,2401v 9

Uji t tdaya t tabel=2.262 Uji t delta Ptdaya 1 (s) tdaya 2 (s) d d2 x 10^-3 tau t test deltaP 1 (P deltaP 2 (P

14.385 15.475 -1.09 1188.1 93.432993 0.024281 24516.63 24516.6314.172 15.353 -1.181 1394.761 32361.95 32361.9514.097 15.156 -1.059 1121.481 36284.6 37265.2714.057 15.064 -1.007 1014.049 44129.93 42168.6

13.82 14.943 -1.123 1261.129 49033.25 49033.25

13.382 14.823 -1.441 2076.481 68646.55 61781.913.352 13.795 -0.443 196.249 73549.88 98066.512.929 13.075 -0.146 21.316 101989.2 119641.112.113 11.504 0.609 370.881 130428.4 17848110.622 10.915 -0.293 85.849 196133 215746.3

total 7.174 8730.296 totalrata2 0.7174 873.0296 rata2

Head run 1Head run 2 d2

d2 total

d2 rata-rata

t tabel=2.262 Uji t tflow t tabel=2.262d d2 x 10^-4 tau t test tflow 1 (s) tflow 2 (s) d d2 tau

0 0 6048396 0.005332 12.76 10.129 2.631 69221.61 2273.3930 0 13.164 13.131 0.033 10.89

-980.665 9.62E+09 13.348 13.294 0.054 29.161961.33 3.85E+10 13.666 13.487 0.179 320.41

0 0 14.137 13.855 0.282 795.24

6864.655 4.71E+11 15.484 15.193 0.291 846.81-24516.63 6.01E+12 16.211 18.655 -2.444 59731.36-17651.97 3.12E+12 19.056 22.679 -3.623 131261.3-48052.58 2.31E+13 24.129 41.149 -17.02 2896804

-19613.3 3.85E+12 50.123 64.298 -14.175 2009306101989.2 3.66E+13 total 33.792 516832710198.92 3.66E+12 rata2 3.3792 516832.7

t test0.0047

rho 996.8 0.9968gravitasi 9.8

No Variasi Bukaan (%) Psuction (kgf/cm2) Pdischarge (kgf/cm2)1 26.67 0 0.422 20 0 0.53 16.67 0 0.534 15 0 0.635 13.33 0 0.776 11.67 0 1.47 10.55 0 1.468 9.55 0 1.79 6.78 0 2

10 5.66 0 2.4

No Variasi Bukaan (%) Psuction (kgf/cm2) Pdischarge (kgf/cm2)1 26.67 0 0.372 20 0 0.473 16.67 0 0.54 15 0 0.565 13.33 0 0.736 11.67 0 17 10.55 0 1.78 9.55 0 1.849 6.78 0 2

10 5.66 0 2.38

Pdischarge (Pa) V(x10 t flow t daya delta P Q (laju alir h (head pump)41187.93 0.005 12.074 14.143 41187.93 4.14 4.216349033.25 0.005 12.169 14.054 49033.25 4.11 5.0195

51975.245 0.005 12.599 13.999 51975.25 3.97 5.320661781.895 0.005 12.91 13.836 61781.90 3.87 6.324575511.205 0.005 13.808 13.338 75511.21 3.62 7.7300

137293.1 0.005 15.391 12.51 137293.10 3.25 14.0545143177.09 0.005 19.897 11.536 143177.09 2.51 14.6568166713.05 0.005 22.089 10.864 166713.05 2.26 17.0661

196133 0.005 26.778 10.375 196133.00 1.87 20.0778235359.6 0.005 41.277 9.376 235359.60 1.21 24.0934

Pdischarge (Pa) V(x10 t flow t daya delta P Q (laju alir h (head pump)36284.605 0.005 11.944 14.43 36284.60 4.19 3.7146091.255 0.005 12.215 14.17 46091.26 4.09 4.72

49033.25 0.005 12.513 14.01 49033.25 4.00 5.0254917.24 0.005 12.818 13.95 54917.24 3.90 5.62

71588.545 0.005 13.355 13.74 71588.55 3.74 7.3398066.5 0.005 14.981 13.1 98066.50 3.34 10.04

166713.05 0.005 21.928 11.43 166713.05 2.28 17.07180442.36 0.005 24.954 10.71 180442.36 2.00 18.47

196133 0.005 27.121 10.17 196133.00 1.84 20.08233398.27 0.005 36.296 9.74 233398.27 1.38 23.89

p listrik p hidrolik efisiensi Pdischarge (kgf/cm2)203.63 17.06 8.3760 0.09204.92 20.15 9.8314 0.1205.73 20.63 10.0262 0.2208.15 23.93 11.4954 0.25215.92 27.34 12.6634 0.29230.22 44.60 19.3739 0.32249.65 35.98 14.4118 0.45265.10 37.74 14.2351 0.55277.59 36.62 13.1928 0.67307.17 28.51 9.2815 0.83

0

p listrik p hidrolik efisiensi199.58 15.19 7.61203.25 18.87 9.28205.57 19.59 9.53206.45 21.42 10.38209.61 26.80 12.79219.85 32.73 14.89251.97 38.01 15.09268.91 36.15 13.45283.19 36.16 12.77295.69 32.15 10.87 Uji t tdaya t tabel=2.262

tdaya 1 (s) tdaya 2 (s) d d2 tau14.143 14.43 -0.287 823.69 91.0009214.054 14.17 -0.116 134.5613.999 14.01 -0.011 1.2113.836 13.95 -0.114 129.9613.338 13.74 -0.402 1616.04

12.51 13.1 -0.59 348111.536 11.43 0.106 112.3610.864 10.71 0.154 237.1610.375 10.17 0.205 420.25

9.376 9.74 -0.364 1324.96total 1.419 8281.19rata2 0.1419 828.119

Uji t delta P t tabel=2.262t test deltaP 1 (P deltaP 2 (P d d2x10^-4 tau t test0.004931 41187.93 36284.6 4903.325 2.4E+11 4887608 0.00165

49033.25 46091.26 2941.995 8.66E+1051975.25 49033.25 2941.995 8.66E+10

61781.9 54917.24 6864.655 4.71E+1175511.21 71588.55 3922.66 1.54E+11137293.1 98066.5 39226.6 1.54E+13143177.1 166713.1 -23535.96 5.54E+12166713.1 180442.4 -13729.31 1.88E+12

196133 196133 0 0235359.6 233398.3 1961.33 3.85E+10

total 25497.29 2.39E+13rata2 2549.729 2.39E+12

Uji t tflow t tabel=2.262tflow 1 (s) tflow 2 (s) d d2 tau t test

12.074 11.944 0.13 169 613.7539 0.00044712.169 12.215 -0.046 21.1612.599 12.513 0.086 73.96

12.91 12.818 0.092 84.6413.808 13.355 0.453 2052.0915.391 14.981 0.41 168119.897 21.928 -2.031 41249.6122.089 24.954 -2.865 82082.2526.778 27.121 -0.343 1176.4941.277 36.296 4.981 248103.6

total 0.867 376693.8rata2 0.0867 37669.38

rho 996.8 0.9968gravitasi 9.8

No Variasi Bukaan (%) Psuction (kgf/cm2) Pdischarge (kgf/cm2)1 46.67 0 0.422 40 0 0.473 36 0 0.54 30 0 0.525 26.67 0 0.556 23.33 0 0.677 21.67 0 0.758 20 0 0.89 18.33 0 1

10 15 0 1.6

No Variasi Bukaan (%) Psuction (kgf/cm2) Pdischarge (kgf/cm2)1 46.67 0 0.422 40 0 0.463 36 0 0.54 30 0 0.525 26.67 0 0.526 23.33 0 0.587 21.67 0 0.678 20 0 0.759 18.33 0 1.04

10 15 0 1.9

V(x10 t flow t daya A t daya B delta P Q (laju alir41187.93 0.005 11.252 16.248 15.427 41187.93 4.44

46091.255 0.005 11.288 16.191 15.305 46091.26 4.4349033.25 0.005 11.349 16.134 15.133 49033.25 4.4150994.58 0.005 11.481 15.989 15.047 50994.58 4.36

53936.575 0.005 11.549 15.889 15.033 53936.58 4.3365704.555 0.005 11.714 15.84 14.891 65704.56 4.2773549.875 0.005 11.837 15.809 14.771 73549.88 4.22

78453.2 0.005 12.046 15.787 14.716 78453.2 4.1598066.5 0.005 12.529 15.375 14.336 98066.5 3.99

156906.4 0.005 14.676 14.638 13.015 156906.4 3.41

V(x10 t flow t daya A t daya B delta P Q (laju alir41187.93 0.005 11.196 16.156 15.354 41187.93 4.4745110.59 0.005 11.222 16.12 15.222 45110.59 4.4649033.25 0.005 11.244 15.576 14.72 49033.25 4.4550994.58 0.005 11.483 15.238 14.577 50994.58 4.3550994.58 0.005 11.493 15.221 14.483 50994.58 4.3556878.57 0.005 11.678 15.195 14.269 56878.57 4.28

65704.555 0.005 11.886 15.018 14.463 65704.56 4.2173549.875 0.005 11.945 14.919 14.301 73549.88 4.19101989.16 0.005 12.927 14.67 13.964 101989.2 3.87186326.35 0.005 16.126 13.925 12.418 186326.3 3.10

h (head pu p listrik p hidrolik efisiensi4.22 363.94 18.30 5.034.72 366.05 20.42 5.585.02 368.82 21.60 5.865.22 371.52 22.21 5.985.52 372.84 23.35 6.266.73 375.22 28.05 7.477.53 377.15 31.07 8.248.03 378.13 32.56 8.61

10.04 388.21 39.14 10.0816.06 418.03 53.46 12.79

h (head pu p listrik p hidrolik efisiensi4.22 365.84 18.39 5.034.62 367.86 20.10 5.465.02 380.55 21.80 5.735.22 386.57 22.20 5.745.22 388.07 22.19 5.725.82 391.37 24.35 6.226.73 390.90 27.64 7.077.53 394.43 30.79 7.81

10.44 402.56 39.45 9.8019.07 438.74 57.77 13.17 Uji t tdayaA t tabel=2.262

tdaya 1 (s) tdaya 2 (s) d d2x10^-416.248 16.156 0.092 84.6416.191 16.12 0.071 50.4116.134 15.576 0.558 3113.6415.989 15.238 0.751 5640.0115.889 15.221 0.668 4462.24

15.84 15.195 0.645 4160.2515.809 15.018 0.791 6256.8115.787 14.919 0.868 7534.2415.375 14.67 0.705 4970.2514.638 13.925 0.713 5083.69

total 5.862 41356.18rata2 0.5862 4135.618

Uji t tdayaB t tabel=2.262tdaya 1 (s) tdaya 2 (s) d d2 x 10^-4

15.427 15.354 0.073 53.2915.305 15.222 0.083 68.8915.133 14.72 0.413 1705.6915.047 14.577 0.47 2209

15.033 14.483 0.55 302514.891 14.269 0.622 3868.8414.771 14.463 0.308 948.6414.716 14.301 0.415 1722.2514.336 13.964 0.372 1383.8413.015 12.418 0.597 3564.09

total 3.903 18549.53rata2 0.3903 1854.953

Uji t delta P t tabel=2.262tau t test deltaP 1 (P deltaP 2 (P d d2 x 10^-4 tau203.3613 0.009115 0.42 0.42 0 0 33.10589

0.47 0.46 0.01 10.5 0.5 0 0

0.52 0.52 0 00.55 0.52 0.03 90.67 0.58 0.09 810.75 0.67 0.08 64

0.8 0.75 0.05 251 1.04 -0.04 16

1.6 1.9 -0.3 900total 0.08 1096rata2 0.008 110

tau t test45.39702 0.027188

Uji t tflow t tabel=2.262t test tflow 1 (s) tflow 2 (s) d d2x10^-2 tau t test0.000764 11.252 11.196 0.056 0.3136 15.15327 0.030865

11.288 11.222 0.066 0.435611.349 11.244 0.105 1.102511.481 11.483 -0.002 0.000411.549 11.493 0.056 0.313611.714 11.678 0.036 0.129611.837 11.886 -0.049 0.240112.046 11.945 0.101 1.020112.529 12.927 -0.398 15.840414.676 16.126 -1.45 210.25

total 1.479 229.6459rata2 0.1479 22.96459

rho 996.8 0.9968gravitasi 9.8

No Variasi Bukaan (%) Psuction (kgf/cm2) Pdischarge (kgf/cm2)1 46.67 0 0.91 89240.5154 30 0 0.98 96105.173 20 0 1.05 102969.8252 19.67 0 1.14 111795.815 19.33 0 1.22 119641.136 19 0 1.56 152983.747 18.89 0 1.6 156906.48 18.78 0 1.73 169655.0459 18.66 0 1.88 184365.02

10 18.33 0 2.33 228494.945

No Variasi Bukaan (%) Psuction (kgf/cm2) Pdischarge (kgf/cm2)1 46.67 0 0.95 93163.1754 30 0 1 98066.53 20 0 1.04 101989.162 19.67 0 1.1 107873.155 19.33 0 1.18 115718.476 19 0 1.2 117679.87 18.89 0 1.2 117679.88 18.78 0 1.24 121602.469 18.66 0 1.42 139254.43

10 18.33 0 1.6 156906.4

V(x10 t flow t daya t daya B delta P Q (laju alir)x10^-5 h (head pump)0.005 8.084 13.607 13.198 89240.52 61.85 9.140.005 8.466 13.142 13.133 96105.17 59.06 9.840.005 8.799 12.839 12.508 102969.8 56.82 10.540.005 8.981 12.826 12.494 111795.8 55.67 11.440.005 9.792 12.672 12.093 119641.1 51.06 12.250.005 11.645 11.835 11.264 152983.7 42.94 15.660.005 12.166 11.542 10.992 156906.4 41.10 16.060.005 12.294 11.397 10.945 169655 40.67 17.370.005 13.668 11.267 10.825 184365 36.58 18.870.005 26.482 10.22 9.331 228494.9 18.88 23.39

V(x10 t flow t daya t daya B delta P Q (laju alir)x10^-5 h (head pump)0.005 8.097 13.47 13.107 93163.17 61.75 9.540.005 8.306 13.618 12.862 98066.5 60.20 10.040.005 8.577 13.154 12.829 101989.2 58.30 10.440.005 8.979 13.094 12.62 107873.2 55.69 11.040.005 9.21 13.061 12.501 115718.5 54.29 11.850.005 9.403 12.782 12.445 117679.8 53.17 12.050.005 9.708 12.735 12.279 117679.8 51.50 12.050.005 9.932 12.572 12.162 121602.5 50.34 12.450.005 10.838 12.566 11.73 139254.4 46.13 14.260.005 12.607 12.169 11.592 156906.4 39.66 16.06

p listrik p hidrolik efisiensi429.87 55.20 12.84438.44 56.76 12.95454.57 58.51 12.87455.05 62.24 13.68465.43 61.09 13.13499.03 65.69 13.16511.53 64.49 12.61515.83 69.00 13.38521.66 67.44 12.93590.45 43.14 7.31

p listrik p hidrolik efisiensi433.54 57.53 13.27435.40 59.03 13.56443.44 59.46 13.41448.16 60.07 13.40450.89 62.82 13.93456.74 62.58 13.70460.70 60.61 13.16465.88 61.22 13.14474.71 64.24 13.53485.11 62.23 12.83 Uji t tdayaA t tabel=2.262

0 tdaya 1 (s) tdaya 2 (s) d d2x10^-213.607 13.47 0.137 1.876913.142 13.618 -0.476 22.657612.839 13.154 -0.315 9.922512.826 13.094 -0.268 7.182412.672 13.061 -0.389 15.132111.835 12.782 -0.947 89.680911.542 12.735 -1.193 142.324911.397 12.572 -1.175 138.062511.267 12.566 -1.299 168.7401

10.22 12.169 -1.949 379.8601total 7.874 975.44rata2 0.7874 97.544

Uji t tdayaB t tabel=2.262tdaya 1 (s) tdaya 2 (s) d d2x10-2

13.198 13.107 0.091 0.828113.133 12.862 0.271 7.344112.508 12.829 -0.321 10.304112.494 12.62 -0.126 1.587612.093 12.501 -0.408 16.646411.264 12.445 -1.181 139.476110.992 12.279 -1.287 165.636910.945 12.162 -1.217 148.108910.825 11.73 -0.905 81.9025

9.331 11.592 -2.261 511.2121total 7.344 1083.047rata2 0.7344 108.3047

Uji t delta P t tabel=2.262tau t test deltaP 1 (P deltaP 2 (P d d2x10^-4 tau t test

31.221 0.079753 0.91 0.95 -0.04 16 113.1147 0.0069050.98 1 -0.02 41.05 1.04 0.01 11.14 1.1 0.04 161.22 1.18 0.04 161.56 1.2 0.36 1296

1.6 1.2 0.4 16001.73 1.24 0.49 24011.88 1.42 0.46 21162.33 1.6 0.73 5329

total 2.47 12795rata2 0.247 1279.5

tau t test

32.90057 0.070588

Uji t tflow t tabel=2.262tflow 1 (s) tflow 2 (s) d d2* tau t test

8.084 8.097 -0.013 0.000169 14.51881 0.5384158.466 8.306 0.16 0.02568.799 8.577 0.222 0.0492848.981 8.979 0.002 4E-069.792 9.21 0.582 0.338724

11.645 9.403 2.242 5.02656412.166 9.708 2.458 6.04176412.294 9.932 2.362 5.57904413.668 10.838 2.83 8.008926.482 12.607 13.875 192.5156

total 24.72 217.5857rata2 2.472 21.75857