FLUIDA RAHAYU
9
NAMA : RAHAYU JATI PERMANA NIM : 1301873 GANJIL PIPA AB BC CD DE EF FA Panjang 625 625 195 625 625 195 Diameter 255 155 105 155 155 210 Luas 0.051071 0.018869 0.008659 0.018869 0.0188692 0.034636 k = 0.053 mm v = 1.13E-06 Elevasi titik simpul pipa Node A B C D E F Elevasi (m dpl 35 30 25 25 27 30 Inlet (L/s) 237.23 0 0 0 0 0 Demand (L/s) 0 17.07784 67 63 82.922164 7.22 Ʃdemand= A B 1 2 F E Run 1 loop pipa k/D Q (ltr/s) Re f K 1 AB 0.000212 125 563380.3 0.0115342 585.5434 BE 0.00053 25 281690.2 0.0137165 27200.48 EF 0.000353 -105 788732.5 0.0106036 6922.626 FA 0.000265 -112.22 632225.4 0.0112065 636.5947 loop pipa k/D Q (ltr/s) Re f K 2 BC 0.000353 75 563380.3 0.0115342 7530.137 CD 0.00053 8 90140.85 0.0182371 33151.3 DE 0.000353 -55 413145.6 0.0124641 8137.247 BE 0.00053 -48 540845.1 0.0116525 23107.41 Run 2 loop pipa k/D Q (ltr/s) Re f K AB 0.000212 143.7524 647898.1 0.0111381 565.4352 ∆Q= ∆Q=
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Transcript of FLUIDA RAHAYU
NAMA : RAHAYU JATI PERMANANIM : 1301873
GANJILPIPA AB BC CD DE EF FA BE
Panjang 625 625 195 625 625 195 195Diameter 255 155 105 155 155 210 110Luas 0.0510705 0.0188692 0.008659 0.018869 0.0188692 0.034636 0.00950332k = 0.053 mmv = 1.13E-06
Elevasi titik simpul pipaNode A B C D E F
Elevasi (m dpl) 35 30 25 25 27 30Inlet (L/s) 237.23 0 0 0 0 0Demand (L/s) 0 17.077836 67 63 82.922164 7.22
Ʃdemand= 237.23
A B C
1 2
F E D
Run 1loop pipa k/D Q (ltr/s) Re f K hl hl/Q
1
AB 0.000212 125 563380.3 0.0115342 585.5434 9.14911591 0.073193BE 0.00053 25 281690.2 0.0137165 27200.48 17.0003027 0.680012EF 0.0003533 -105 788732.5 0.0106036 6922.626 -76.3219471 0.726876FA 0.000265 -112.22 632225.4 0.0112065 636.5947 -8.01684639 0.071439
-58.1893748 1.55151918.7523841
loop pipa k/D Q (ltr/s) Re f K hl hl/Q
2
BC 0.0003533 75 563380.3 0.0115342 7530.137 42.3570181 0.56476CD 0.00053 8 90140.85 0.0182371 33151.3 2.12168329 0.26521DE 0.0003533 -55 413145.6 0.0124641 8137.247 -24.615172 0.447549BE 0.00053 -48 540845.1 0.0116525 23107.41 -53.23948 1.109156
-33.3759506 2.3866756.9921438
Run 2loop pipa k/D Q (ltr/s) Re f K hl hl/Q
1
AB 0.000212 143.75238 647898.1 0.0111381 565.4352 11.6845759 0.081283
∆Q=
∆Q=
1 BE 0.00053 43.752384 492984.7 0.0119256 23648.91 45.2704337 1.034696EF 0.0003533 -86.24762 647869.5 0.0111382 7271.624 -54.0910723 0.62716FA 0.000265 -93.46762 526578.2 0.0117306 666.3698 -5.82153668 0.062284
-2.95759933 1.8054230.81908753
loop pipa k/D Q (ltr/s) Re f K hl hl/Q
2
BC 0.0003533 81.992144 615903.5 0.01128 7364.192 49.5073398 0.603806CD 0.00053 14.992144 168925.6 0.015587 28333.95 6.36846289 0.424787DE 0.0003533 -48.00786 360622.4 0.0128951 8418.604 -19.4028138 0.404159BE 0.00053 -41.00786 462060.4 0.0121203 24035.04 -40.4183895 0.985626
-3.94540058 2.4183770.8157124
Run 3loop pipa k/D Q (ltr/s) Re f K hl hl/Q
1
AB 0.000212 144.57147 651589.8 0.0111223 564.6326 11.8013356 0.08163BE 0.00053 44.571472 502213.8 0.0118704 23539.51 46.7639668 1.049191EF 0.0003533 -85.42853 641716.7 0.0111648 7288.991 -53.195303 0.622688FA 0.000265 -92.64853 521963.6 0.0117565 667.8378 -5.73255221 0.061874
-0.36255277 1.8153820.09985576
loop pipa k/D Q (ltr/s) Re f K hl hl/Q
2
BC 0.0003533 82.807856 622030.9 0.0112521 7345.989 50.3724837 0.608306CD 0.00053 15.807856 178116.7 0.0153819 27961.14 6.9871616 0.442006DE 0.0003533 -47.19214 354495 0.0129504 8454.749 -18.8295592 0.398998BE 0.00053 -40.19214 452869.3 0.0121813 24156.07 -39.021925 0.970884
-0.49183889 2.4201930.10161149
Run 4loop pipa k/D Q (ltr/s) Re f K hl hl/Q
1
AB 0.000212 144.67133 652039.8 0.0111204 564.5352 11.8156039 0.081672BE 0.00053 44.671327 503338.9 0.0118637 23526.34 46.9474643 1.050953EF 0.0003533 -85.32867 640966.6 0.0111681 7291.123 -53.0865375 0.622142FA 0.000265 -92.54867 521401 0.0117596 668.0178 -5.72174421 0.061824
-0.04521 1.8165910.01244459
∆Q=
∆Q=
∆Q=
∆Q=
∆Q=
loop pipa k/D Q (ltr/s) Re f K hl hl/Q
2
BC 0.0003533 82.909468 622794.2 0.0112487 7343.737 50.4807025 0.608865CD 0.00053 15.909468 179261.6 0.0153573 27916.38 7.06594845 0.444135DE 0.0003533 -47.09053 353731.7 0.0129574 8459.307 -18.7586667 0.398353BE 0.00053 -40.09053 451724.3 0.012189 24171.37 -38.8494459 0.969043
-0.06146174 2.4203960.01269663
Run 5loop pipa k/D Q (ltr/s) Re f K hl hl/Q
1
AB 0.000212 144.68377 652095.9 0.0111201 564.523 11.8173826 0.081677BE 0.00053 44.683772 503479.2 0.0118629 23524.7 46.9703544 1.051173EF 0.0003533 -85.31623 640873.1 0.0111685 7291.389 -53.0729892 0.622074FA 0.000265 -92.53623 521330.9 0.01176 668.0403 -5.72039787 0.061818
-0.00565 1.8167420.00155499
loop pipa k/D Q (ltr/s) Re f K hl hl/Q
2
BC 0.0003533 82.922164 622889.6 0.0112482 7343.456 50.4942317 0.608935CD 0.00053 15.922164 179404.7 0.0153543 27910.82 7.07581967 0.444401DE 0.0003533 -47.07784 353636.4 0.0129583 8459.877 -18.7498166 0.398273BE 0.00053 -40.07784 451581.3 0.01219 24173.28 -38.8279172 0.968813
-0.00768244 2.4204210.001587
RESUMEPipa Q (L/s) hlAB 144.68377 11.81738BE 44.683772 46.97035EF 85.316228 -53.07299FA 92.536228 -5.720398BC 82.922164 50.49423CD 15.922164 7.07582DE 47.077836 -18.74982
∆Q=
∆Q=
∆Q=
PIPA Diameter Luas Panjang volume(m3volume(ltr)LOOP 1 AB 250 0.049087 600 29.45243 29452.43113
BE 100 0.007854 240 1.884956 1884.955592EF 150 0.017671 600 10.60288 10602.87521FA 200 0.031416 220 6.911504 6911.503839
LOOP 2 BC 150 0.017671 600 10.60288 10602.87521CD 100 0.007854 220 1.727876 1727.87596DE 150 0.017671 600 10.60288 10602.87521EB 100 0.007854 240 1.884956 1884.955592
TRY K/D QAB 0.00024 120BE 0.0006 20EF 0.0004 -100FA 0.0003 -140.48
velocity k/Q2 2k/Q kQQ Kq0^1,8521,852kQ0^0,8522.546479 3.392E-09 4.50642E-07 0.828125 405.2782 6.0046013983.183099 0.0000000848 4.50642E-07 0.033125 20.57125 1.523918493
-5.941785 4.807256E-09 4.50642E-07 0.584325 -293.439 5.175712388-3.572074 4.208578E-09 4.50642E-07 0.667446 -331.899 5.4774285
9.720783E-08 1.802568E-06 0 -199.489 18.18166078
DELTA Q 0.0539274214 delta q -10.971991814.164037234
velocity k/Q2 2k/Q K 0.064.244132 9.422222E-09 4.50642E-07 260.481.018592 8.28125E-07 4.50642E-07 662.73 120
-3.112363 1.752066E-08 4.50642E-07 31572.85 20-6.11155 2.300347E-08 4.50642E-07 10903.77 -100
8.780714E-07 1.802568E-06 818.845 -140.48
delta Q 0.487122510110.266106899
velocity k/Q^2 2k/Q2.9285 2.564754E-06 0.000450642
5.570727 2.768678E-05 0.000450642-4.880617 7.124948E-06 0.000450642-2.975167 6.066714E-06 0.000450642
4.344319E-05 0.0018025678
DELTA Q 0.02410072680.0241007268
velocity k/Q^2 2k/Q4.639806 7.883724E-06 0.0004506421.908859 0.0002358025 0.000450642
-2.716689 2.299594E-05 0.000450642-5.221282 3.151677E-05 0.000450642
0.0002981989 0.0018025678
DELTA Q 0.1654300776
velocity k/Q^2 2k/Q2.945186 2.535775E-06 0.0004506425.675016 2.667853E-05 0.000450642
-4.834266 7.26223E-06 0.000450642-2.949094 6.174458E-06 0.000450642
4.265099E-05 0.0018025678
DELTA Q 0.0236612427
velocity k/Q^2 2k/Q4.685966 7.729169E-06 0.0004506422.012719 0.0002120947 0.000450642
-2.670529 2.379778E-05 0.000450642-5.117423 3.280904E-05 0.000450642
0.0002764307 0.0018025678
DELTA Q 0.1533538639
velocity k/Q^2 2k/Q2.94722 2.532275E-06 0.0004506425.68773 2.655939E-05 0.000450642
-4.828615 7.279238E-06 0.000450642-2.945916 6.187789E-06 0.000450642
4.25587E-05 0.0018025678
DELTA Q 0.0236100384
velocity k/Q^2 2k/Q4.691716 7.710235E-06 0.0004506422.025656 0.0002093942 0.000450642
-2.664779 2.390059E-05 0.000450642-5.104485 3.297556E-05 0.000450642
0.0002739806 0.0018025678
DELTA Q 0.1519945896
velocity2.9474745.689315
-4.827911-2.94552
velocity4.6924352.027273
-2.664061-5.102869
1,852kQ0^0,852
h=Kq^2 h/Q4.166667E-09 0.000001 9.543312 0.079528
0.00000015 0.000006 12.62914 0.6314570.000000006 -1.2E-06 -109.0377 1.090377
3.040341E-09 -8.54E-07 -16.1596 0.1150311.63207E-07 4.946E-06 -103.0248 1.916392
DELTA Q 0.032999 -26.8798828.42882
