Pengolahan Data ALF - Print

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PENGOLAHAN DATA ALF Pengukuran densitas air keran : Pengukuran Viskositas air k Massa piknometer kosong (g) 18.4 akt! temp!" a#!a $m Massa piknometer kosong % a#!a $m (g) &8.' akt! temp!" air keran Massa a#!a $m (g) 1 .& Temperat!re a#!a $m () Massa piknometer kosong % air keran (g) &8.' *iskositas air (+iterat!r) (Pa.s) Massa etano+ (g) 1 .& *iskositas air keran (Pa.s) Temperat!re a#!a $m ( ) &, Densitas air (+iterat!r) (kg-m ) .//0 8 Densitas air keran (kg-m ) .//0 8

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Transcript of Pengolahan Data ALF - Print

Sheet1PENGOLAHAN DATA ALFPengukuran densitas air keran : Pengukuran Viskositas air keran :

Massa piknometer kosong (g)18.4Waktu tempuh aqua dm164Massa piknometer kosong + aqua dm (g)28.6Waktu tempuh air keran 166Massa aqua dm (g)10.2Temperature aqua dm (C )25Massa piknometer kosong + air keran (g)28.6Viskositas air (literatur) (Pa.s)0.0008937Massa etanol (g) 10.2Viskositas air keran (Pa.s)0.0009045988Temperature aqua dm (C )25Densitas air (literatur) (kg/m3)0.99708Densitas air keran (kg/m3)0.99708

3. Pengukuran dan pengolahan data Head loss dari masing-masing komponen dalam SOLTEQ

Tabel C.3 Karakterisasi Venturimeter

Nama alat : VenturimeterPersamaan matematis : Q = a . Akar(dh) + b Diameter : 2.5cm0.025mLuas penampang0.0004908739m2a = 36.948Densitas air keran0.99708kg/m3b = 160.62Viskositas air keran 0.0009045988Pa.sRun waktu (s)Volume (mL)Debit (mL/s)Q rata-ratav (laju alir linear)dh (mmH2O) akar dh NREt1t2V1V2Q1Q2mL/s m/s11.870.96450220240.64229.17234.900.47910510.2513.1921.071.27285325266.36255.91261.130.53213411.5814.6630.920.99340350369.57353.54361.550.73720814.4220.3040.901.14430545477.78478.07477.920.97429717.2326.8350.851.27450655529.41515.75522.581.06535318.7929.3461.050.92580540552.38586.96569.671.16144221.0231.9870.911.18640830703.30703.39703.341.43351022.5839.4880.981.18770860785.71728.81757.261.54357824.0442.5191.020.64800565784.31882.81833.561.69867325.9446.79100.730.93625755856.16811.83834.001.69978327.9846.82

Tabel C.4 Karakterisasi OrificemeterNama alat : OrificemeterPersamaan matematis : Q = a . Akar(dh) + b Diameter : 2.5cm0.025mLuas penampang0.0004908739m2a = 0.0424Densitas air keran0.99708kg/m3b = 2.2664Viskositas air keran 0.0009045988Pa.sRun waktu (s)Volume (mL)Debit (mL/s)Q rata-ratav (laju alir linear)dh (mmH2O) akar dh NREt1t2V1V2Q1Q2mL/s m/s11.111.06370330333.33311.32322.330.65725015.8118.0921.131.51450565398.23374.17386.200.78734118.4721.6831.271.25725660570.87528.00549.431.11962024.9030.8441.191.08690700579.83648.15613.991.25180528.3734.4751.031.14780740757.28649.12703.201.433105032.4039.4861.021.05705815691.18776.19733.681.495122835.0441.1970.960.95790820822.92863.16843.041.717137637.0947.3380.890.85725730814.61858.82836.721.705152539.0546.9790.720.82605845840.281030.49935.381.906167340.9052.51100.730.597854801075.34813.56944.451.924177542.1353.02Tabel C.5 Karakterisasi Tabung pitotNama alat : Tabung pitot Persamaan matematis : Q = a . Akar(dh) + b Diameter : 2.5cm0.025mLuas penampang0.0004908739m2a = 0.0089Densitas air keran0.99708kg/m3b = 5.1571Viskositas air keran 0.0009045988Pa.sRun waktu (s)Volume (mL)Debit (mL/s)Q rata-ratav (laju alir linear)dh (mmH2O) akar dh NREt1t2V1V2Q1Q2mL/s m/s12.002.04290290145.00142.16143.580.292244.908.0622.011.88315305156.72162.23159.480.325325.668.9531.441.35245265170.14196.30183.220.373658.0610.2941.711.17470410274.85350.43312.640.637768.7217.5551.551.33570540367.74406.02386.880.788869.2721.7261.200.82650480541.67585.37563.521.14810710.3431.6371.071.20600750560.75625.00592.871.20812010.9533.2880.860.94695700808.14744.68776.411.58213211.4943.5890.960.90750690781.25766.67773.961.57713511.6243.45100.920.95695735755.43773.68764.561.55814011.8342.92Tabel C.6 Karakterisasi 6 mm smooth bore pipeNama alat : 6 mm smooth bore pipePersamaan matematis : h = 4L/D . f . hv = ax+bDiameter : 0.6cm0.006ma = 339.37Luas penampang0.0000282743m2f.L = 50.9055Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s1839.11497.2317.59372561.03116.3015.78211510.72556.8419.69525572.49130.2519.79313511.62589.9220.86580576.19137.9822.21414311.96602.4521.31632079.50140.9123.16515212.33616.1521.79662681.40144.1224.23615712.53623.5822.05683582.67145.8624.82716312.77632.3422.36701083.73147.9125.52816612.88636.6622.52727285.28148.9225.87917013.04642.3622.72732585.59150.2526.331017313.15646.6022.87746386.39151.2426.68

Tabel C.7 Karakterisasi 10 mm smooth bore pipe

Nama alat : 10 mm smooth bore pipePersamaan matematis : h = 4L/D . f . hv = ax+bDiameter : 1cm0.01ma = 1014.8Luas penampang0.0000785398m2f.L = 253.7Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s132418.00825.6810.51479269.22115.885.6388676823234818.65849.8810.82530072.80119.275.9741386666337519.36876.1111.16563475.06122.956.348722457440220.05901.4311.48597077.27126.516.7208384457540920.22907.8511.56608077.97127.416.8169411612641420.35912.4011.62618078.61128.056.8854967192741820.45916.0211.66625079.06128.566.9402886562843220.78928.5711.82633079.56130.327.1317028134944020.98935.6511.91646580.41131.317.24084006381044221.02937.4111.94654780.91131.567.2680976012

Tabel C.8 Karakterisasi 17 mm smooth bore pipe

Nama alat : 17 mm smooth bore pipePersamaan matematis : h = 4L/D . f . hv = ax+bDiameter : 1.7cm0.017ma = 639.12Luas penampang0.0002269801m2f.L = 271.626Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s1160040.001638.547.22163040.37135.272.6587810582159039.871633.917.20160540.06134.892.64379031383157139.641625.097.16159239.90134.162.61529509424156039.501619.957.14158139.76133.732.59879009485154339.281611.987.10156239.52133.072.57327099566152239.011602.077.06154639.32132.262.54172803227149638.681589.707.00152239.01131.242.50264454978146838.311576.266.94149138.61130.132.46051622289143637.891560.756.88145838.18128.852.412319333910138837.261537.156.77142237.71126.902.3399197133

Tabel C.9 Karakterisasi 17 mm artificially roughened

Nama alat : 17 mm artificially roughened Persamaan matematis : h = 4L/D . f . hv = ax+bDiameter : 1.7cm0.017ma = 9536.2Luas penampang0.0002269801m2f.L = 4052.885Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s120514.32689.633.04312855.9356.930.4709847916232518.03826.713.64500570.7568.250.6768218672337719.42878.023.87586076.5572.480.7634448786440620.15905.103.99625079.0674.720.8112657064543520.86931.234.10680282.4776.880.8587839615646621.59958.224.22722084.9779.100.9092783666749422.23981.834.33769087.6981.050.9546438469851122.61995.844.39796089.2282.210.9820835845954323.301021.604.50850092.2084.341.03353816441056023.661034.974.56870193.2885.441.0607752662

Tabel C.10 Karakterisasi sudden enlargement

Nama alat : sudden enlargementDiameter : 0.1cm0.001mLuas penampang0.0000007854m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s132418.00825.681051.2966025.691158.7756388.68234818.65849.881082.1074227.241192.7259741.39337519.36876.111115.5078928.091229.5563487.22440220.05901.431147.7384028.981265.0767208.38540920.22907.851155.9185529.241274.0868169.41641420.35912.401161.7086329.381280.4768854.97741820.45916.021166.3287529.581285.5669402.89843220.78928.571182.2989429.901303.1671317.03944020.98935.651191.3090330.051313.1072408.401044221.02937.411193.5492030.331315.5772680.98

Tabel C.11 Karakterisasi sudden contraction

Nama alat : sudden contractionDiameter : 0.25cm0.0025mLuas penampang0.0000049087m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s132418.00825.68168.21350759.22463.511443.55234818.65849.88173.14392362.63477.091529.38337519.36876.11178.48419264.75491.821625.27440220.05901.43183.64446566.82506.031720.53540920.22907.85184.95454967.45509.631745.14641420.35912.40185.87463968.11512.191762.69741820.45916.02186.61468368.43514.221776.71843220.78928.57189.17477769.12521.271825.72944020.98935.65190.61488369.88525.241853.661044221.02937.41190.97495670.40526.231860.63

Tabel C.12 Karakterisasi 450 Y

Nama alat : 45 YDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s121014.49696.051.42164.0039.070.10247521.79965.881.97456.7154.220.20355823.621033.412.11527.2158.010.23462124.921081.362.20557.4260.700.25569626.381135.382.31597.6863.740.27670626.571142.352.33648.0064.130.28771426.721147.902.34678.1964.440.28872026.831152.042.35658.0664.670.28972426.911154.792.35728.4964.830.281072626.941156.162.36648.0064.900.28

Tabel C.13 Karakterisasi 450 elbow

Nama alat : 45 elbowDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s121014.49696.051.42123.4639.070.10247521.79965.881.97325.6654.220.20355823.621033.412.11355.9258.010.23462124.921081.362.20376.0860.700.25569626.381135.382.31376.0863.740.27670626.571142.352.33446.6364.130.28771426.721147.902.34466.7864.440.28872026.831152.042.35527.2164.670.28972426.911154.792.35426.4864.830.281072626.941156.162.36497.0064.900.28

Tabel C.14 Karakterisasi 900T

Nama alat : 90 TDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s194130.681294.032.6412010.9572.640.35285529.241240.992.5311310.6369.660.33376027.571179.212.4010110.0566.200.29465925.671109.112.26869.2762.260.26557223.921044.292.13768.7258.620.23649322.20981.002.00607.7555.070.20739619.90895.881.83517.1450.290.17827616.61774.451.58406.3243.470.13910210.10533.781.09153.8729.960.0610234.80337.820.6931.7318.960.02

Tabel C.15 Karakterisasi 900 elbow

Nama alat : 90 elbowDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s194130.681294.032.6411810.8672.640.35285529.241240.992.5310610.3069.660.33376027.571179.212.40999.9566.200.29465925.671109.112.26849.1762.260.26557223.921044.292.13788.8358.620.23649322.20981.002.00637.9455.070.20739619.90895.881.83527.2150.290.17827616.61774.451.58386.1643.470.13910210.10533.781.09174.1229.960.0610234.80337.820.6942.0018.960.02

Tabel C.16 Karakterisasi 900 bend

Nama alat : 90 bendDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s121014.49696.051.42103.1639.070.10247521.79965.881.97133.6154.220.20355823.621033.412.11143.7458.010.23462124.921081.362.20153.8760.700.25569626.381135.382.31164.0063.740.27670626.571142.352.33184.2464.130.28771426.721147.902.34184.2464.440.28872026.831152.042.35194.3664.670.28972426.911154.792.35164.0064.830.281072626.941156.162.36164.0064.900.28

Tabel C.17 Karakterisasi gate valve

Nama alat : gate valveDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s194130.681294.032.64869.2772.640.35285529.241240.992.53768.7269.660.33376027.571179.212.40738.5466.200.29465925.671109.112.26668.1262.260.26557223.921044.292.13567.4858.620.23649322.20981.002.00507.0755.070.20739619.90895.881.83416.4050.290.17827616.61774.451.58335.7443.470.13910210.10533.781.09153.8729.960.0610234.80337.820.6952.2418.960.02

Tabel C.18 Karakterisasi globe valve setengah terbuka

Nama alat : globe valve setengah terbukaDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s121314.59699.861.4352622.9339.290.10232117.92822.601.6879328.1646.180.14344020.98935.651.91106632.6552.520.19453023.021011.232.06128735.8756.770.22569426.341133.972.31167040.8763.660.27678127.951193.182.43189343.5166.980.30787729.611254.802.56211045.9370.440.33891830.301280.092.61222247.1471.860.35996431.051307.792.66231648.1273.410.3610101831.911339.492.73246049.6075.190.38

Tabel C.19 Karakterisasi globe valve terbuka penuh

Nama alat : globe valve terbuka penuhDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s194130.681294.032.64164640.5772.640.35285529.241240.992.53150138.7469.660.33376027.571179.212.40136036.8866.200.29465925.671109.112.26116034.0662.260.26557223.921044.292.13101431.8458.620.23649322.20981.002.0086029.3355.070.20739619.90895.881.8369626.3850.290.17827616.61774.451.5848922.1143.470.13910210.10533.781.0918513.6029.960.0610234.80337.820.69426.4818.960.02

Tabel C.20 Karakterisasi inline Y strainer

Nama alat : inline Y strainerDiameter : 2.5cm0.025mLuas penampang0.0004908739m2Densitas air keran0.99708kg/m3Viskositas air keran 0.0009045988Pa.sRun dh venturimeter Akar dhQ v dh (mmH2O) akar dh NREhv (mm)(mmH2O) mL/s m/s194130.681294.032.64141137.5672.640.35285529.241240.992.53128735.8769.660.33376027.571179.212.40116934.1966.200.29465925.671109.112.2698831.4362.260.26557223.921044.292.1386729.4458.620.23649322.20981.002.0073627.1355.070.20739619.90895.881.8359324.3550.290.17827616.61774.451.5842320.5743.470.13910210.10533.781.0916112.6929.960.0610234.80337.820.69406.3218.960.02

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