wwc kelompok 21

data percobaanWETTED WALL COLUMNEMAIL BU [email protected] (m2)[email protected] (L/s)0.07v (m/s)0.0383030844Laju alir air = 70 ml/sD (m)0.04825delta hT udara inT dryTwetrelative humidity %Waktu (menit)1282927.57252252927.5715324.528.527715Re2196.6271740207A (m2)0.0018275291TRANSISIQ (L/s)0.0832v (m/s)0.0455259518Laju alir air = 83,2 ml/sD (m)0.04825delta hT udara inT dryTwetrelative humidity %Waktu (menit)T dry sebelum281272928695T wet sebelum27226.52927.5705324.128.727.8695Re3389.9871291376A (m2)0.0018275291TURBULENQ (m3/s)0.1284v (m/s)0.0702588006Laju alir air = 1284 ml/sD (m)0.04825delta hT udara inT dryTwetrelative humidity %Waktu (menit)127292868522429286853252928685

laminerPENGOLAHAN DATA WETTED WALL COLUMNdengan data T in dan T wetfluida yang digunakan dalam manometer adalah Unknown fluid, dimana density-nya 0.766 gr/mL.1). laminer dengan Qair = 30 ml/detik dan humidity in = 68 % (kg uap air/kg udara kering)delta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAiTin dryTout dryTwetTbulkTint1282927.57228.5028.000.02030.02050.02090.031670.031970.0325882.484.281.583.382.39464240152252927.57127.0027.250.02070.02090.02110.032270.032580.032887784.281.580.681.0486238223324.528.5277126.5026.750.02030.02050.02060.031670.031970.0321276.183.380.679.780.1485980982ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.02030.02050.02060.031670.031970.03212ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!cari humidity chart delta PPtPA0PALPAi udaraQudarav udaraGkGDABPBMShReSc750.71.000070.031670.031970.032581.173795052.00.03847.490E-062.263E+100.967801,586.596.986E-121501.41.000150.032280.032580.032881.1856135073.90.05521.838E-052.250E+100.96749.401E-112,277.486.957E-122252.01.000220.031680.031980.032131.18771850101.20.07583.997E-052.241E+100.96822.050E-103,126.476.972E-12ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!1851101.3ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!atmatm.gr. Liter...mL detik...cm det...gmol... det...gmol cm2.det.atmcm2/detatmERROR:#REF!ERROR:#REF!ERROR:#REF!ngarang...gr.... cm.det2atmatmlog Shlog ReLog Sc-10.41807282213.2004644014-11.1557708305-10.02683780873.3574548004-11.157598743-9.68828843933.4950538666-11.1566390556tekanan (kg/m.det2)rho (kg/m3)g (m/s2)h (m)h (mm)Cairan yang dipakai pada percobaan ini ERROR:#REF!ERROR:#REF!ERROR:#REF!Hg101292.8136009.80.76760bukanlah Hg atau Air, tapi cairan Unknown yangAir101292.810009.810.33610336density-nya sudah saya hitung sebesar 0.766 gr/mLUnknown101292.87669.813.493472584913493.5Anggap aja zat unknown ini sebagai zat A1 atm

diameter kolom = 4.825cmmasa jenis air =1gr/mlDebit =28ml/detLaju Alir =1.5321233777cm/sviskositas air =0.01gr/cm.detRe Number air =739.25--> Laminer

mencari variabel a dan b

untuk Sc konstanUntuk Re konstan

perhitungan menggunakan kelima datauntuk Sc konstan:log Sh = a log Re + (log k + b log Sc).1yB1 x + A1Sh = k.Re-0.201Sc-14.87A1 = 2.34k = Sh/(Rea.Scb)B1 =-17.86ShReSckuntuk Re konstan:01586.588863002500log Sh = b log Sc + (log k + a log Re)20.00000000012277.481198348900 yB2 x + A20.00000000023126.467126090200A2 =168.65ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!B2 =1867.8ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!rata-rataERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!A1 - A2 = 166.31 persamaan 2 dikurangi dengan persamaan 1 menjadi:b log Sc - a log Re = A1 - A2rupanya nilai k -nya ga bisa di carilog Sc = (a/b) log Re +166.31/b3hal ini karena komputernya ga sanggung menghitungIni karena nilai Sc yang kecil, sehingga kalau di pangkatkanhubungan antara Re dan Scakan sangat mendekati nol

untuk aliran transisi dan turbulen, metode perhitungannyamasih belum bener. Sebaiknya copy perhitungan aliranlaminer ini kemudian ganti angka-angkanya dengandata pada aliran transisi dan turbulen

penjelasan perhitungan data ada di file WORD:PENGOLAHAN DATA DAN PEMBAHASAN.Kalau ada yang bingung harap dipahami sendiri ya

-11.194maka b = -14.85710.0136maka a = -0.2021

a3=11.163-11.151b=0.00390.0017

transisiPENGOLAHAN DATA WETTED WALL COLUMNdengan data T wet2). Transisi dengan Qair = 176 ml/sdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAiTin dryTout dryTwetTbulkTint02729286928.00ERROR:#DIV/0!0.01990.02010.02030.031070.031370.0316780.684.282.482.4ERROR:#DIV/0!0.526.52927.570ERROR:#VALUE!ERROR:#VALUE!0.02050.02070.02100.031970.032270.03273ERROR:#VALUE!84.281.5ERROR:#VALUE!ERROR:#VALUE!124.128.727.869ERROR:#VALUE!ERROR:#VALUE!0.02070.02090.02110.032270.032580.03288ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!1.5ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.02070.02090.02110.032270.032580.03288ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!

delta PPtPA0PALPAi udarav udaraQudaraGkGDABPBMShReSc0.00001.000000.031070.03140.031671.1775551.98289500.03861.283E-05ERROR:#DIV/0!0.9685ERROR:#DIV/0!1,591.76ERROR:#DIV/0!375.34001.000040.031970.03230.03273ERROR:#VALUE!73.87021350ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!0.9675ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!750.68001.000070.032280.03260.03288ERROR:#VALUE!101.22961850ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!0.9673ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!1126.02001.000110.032280.03260.03288ERROR:#REF!101.28431851ERROR:#REF!ERROR:#REF!ERROR:#REF!0.9674ERROR:#REF!ERROR:#REF!ERROR:#REF!...gr.... cm.det2atmatmatmatm.gr. Liter...cm det...mL detik...gmol... det...gmol cm2.det.atmcm2/detatmERROR:#DIV/0!ERROR:#VALUE!ERROR:#DIV/0!

log Shlog ReLog ScERROR:#DIV/0!3.201876737ERROR:#DIV/0!ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!ERROR:#VALUE!ERROR:#REF!ERROR:#REF!ERROR:#REF!

diameter kolom = 4.8254.825masa jenis air =1gr/ml1debit = 83ml/det12.4352331606laju alir = 4.5416514409viskositas air =0.01gr/cm.det0.01Re Number air =2191.35--> Transisi6000.00


untuk Sc konstanB12.3134A1-17.857

log k + b log Sc = -17.857

B1334.28A23716.7

log k + a log Re = 3716.7

untuk Re dan Sc

Untuk Re konstan

b log Sc - a log Re = -3734.557log Sc = (a/b) log Re + (A1-A2)/b-3734.557/b -11.162--> b =334.5777638416a/b = 0.0041--> a = 1.3717688318

mencari harga k

Sh rata-rata = sigma Sh/n =ERROR:#DIV/0!

Re rata-rata = sigma Re/n =ERROR:#VALUE!

Sc rata-rata = sigma Sc/n =ERROR:#DIV/0!

Sh = k.Re1.372.Sc334.6

maka k = Sh/(Rea.Scb) = ERROR:#DIV/0!~0

dengan data Humidity alat

2). Transisi dengan Qair = 5.689 ml/detikdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAi1026.22624.186.526.1025.090.010.020.031.586E-023.122E-024.610E-022026.2262590.426.1025.550.010.020.031.586E-023.122E-024.610E-023025.425.22593.225.3025.150.010.020.031.586E-023.122E-024.610E-024025.2252594.225.1025.050.010.020.031.586E-023.122E-024.610E-025025.22524.895.925.1024.950.010.020.031.586E-023.122E-024.610E-02 (mmHg)0C0C0C%0C0C(kg uap air/kg udara kering)fraksi mol

delta hPtPA0PALPAiudaraQudaraGkGDABPBMShReSc151.01321.606E-025.015E-042.312E-051.18111.632.634E-024.390E-063.990E+111.0132.597E-151.412E+033.819E-13301.02631.627E-025.080E-042.342E-051.18112.253.635E-025.982E-063.953E+111.0263.578E-151.949E+033.855E-13451.03951.648E-025.145E-042.372E-051.18432.684.342E-027.054E-063.891E+111.0394.280E-152.328E+033.906E-13501.05261.669E-025.210E-042.402E-051.18512.964.799E-027.699E-063.840E+111.0524.733E-152.573E+033.956E-13601.06581.690E-025.275E-042.432E-051.18513.255.269E-028.348E-063.789E+111.0665.199E-152.825E+034.008E-13 (mmHg)atmatmatmatmgr/literLiter/detikgr/cm2detcm2/detatm2.039E-141.109E+041.954E-12

log Shlog ReLog Sc-14.58551012283.1498033826-12.4180284113 -14.44640682533.2897982964-12.413984528-14.36852270293.3669131481-12.40826868-14.32488092023.410361196-12.4027579518-14.28409443613.450952846-12.3970220332

turbulenPENGOLAHAN DATA WETTED WALL COLUMNdengan data T wet3). Turbulen dengan Qair = 43.5 ml/detikdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAiTin dryTout dryTwetTbulkTint02429286826.5027.240.01960.01990.02020.030610.031070.0315275.284.282.479.781.0376121760.52529286827.0027.500.02050.02070.02100.031970.032270.032737784.282.480.681.49454497361ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.02140.02160.02170.033330.033630.03378ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!1.5ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.02140.02160.02170.033330.033630.03378ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!

delta PPtPA0PALPAi udarav udaraQudaraGkGDABPBMShReSc0.00001.00000.030610.031070.031521.189451.98289500.03901.296E-052.250E+100.96876.637E-111,607.836.934E-12konstanta yg digunakan:375.34001.00000.031970.032270.032731.185573.870213500.05521.355E-052.254E+100.96756.920E-112,277.146.944E-12viskositas/miu = 0.018 cP = 1.8 E-04 gr/cm.det750.68001.00010.033330.033630.03378ERROR:#REF!101.22961850ERROR:#REF!ERROR:#REF!ERROR:#REF!0.9664ERROR:#REF!ERROR:#REF!ERROR:#REF!cari lagi!dari psychrometric chart1126.02001.00010.033330.033630.03378ERROR:#REF!101.28431851ERROR:#REF!ERROR:#REF!ERROR:#REF!0.9664ERROR:#REF!ERROR:#REF!ERROR:#REF!...gr.... cm.det2atmatmatmatm.gr. Liter...cm det...mL detik...gmol... det...gmol cm2.det.atmcm2/detatmERROR:#REF!ERROR:#REF!ERROR:#REF!

log Shlog ReLog Sc-10.17800746793.2062393501-11.1590371792-10.1598986783.3573904342-11.1584182399ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!

diameter kolom = 4.825cmmasa jenis air =1gr/mldebitr air =160ml/detlaju alir air = 8.7549907295viskositas air =0.01gr/cm.detRe Number air =4224.28--> Turbulen



log k + b log Sc = -26.182

B1-440.55A2-4922.2

log k + a log Re = -4922.2

untuk Re dan Sc

Untuk Re konstan

b log Sc - a log Re = 4896.018log Sc = (a/b) log Re + (A1-A2)/b-445.3872/b = -11.113--> b =-440.566723657a/b = -0.0112--> a = 4.934347305

mencari harga k

Sh rata-rata = sigma Sh/n =ERROR:#REF!

Re rata-rata = sigma Re/n =ERROR:#REF!

Sc rata-rata = sigma Sc/n =ERROR:#REF!

Sh = k.Re4.934.Sc-440.567

maka k = (Rea.Scb)/Sh = ERROR:#REF!~0

dengan data alat humidity3). Turbulen dengan Qair = 36.259 ml/detikdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAi10262726.194.426.5026.300.010.020.031.586E-023.122E-024.610E-022025.626.825.994.326.2026.050.010.020.031.586E-023.122E-024.610E-023024.826.825.995.825.8025.850.010.020.031.586E-023.122E-024.610E-024024.426.825.995.325.6025.750.010.020.031.586E-023.122E-024.610E-02502526.825.894.725.9025.850.010.020.031.586E-023.122E-024.610E-02 (mmHg)0C0C0C%0C0C(kg uap air/kg udara kering)fraksi molfraksi molfraksi mol

delta hPtPA0PALPAiQudaraGkGDABPBMShReSc151.01321.606E-025.015E-042.312E-051.17951.632.630E-024.384E-064.028E+111.0132.580E-151.410E+033.788E-13301.02631.627E-025.080E-042.342E-051.18072.253.634E-025.980E-063.969E+111.0263.568E-151.948E+033.841E-13451.03951.648E-025.145E-042.372E-051.18232.684.334E-027.042E-063.913E+111.0394.260E-152.324E+033.891E-13601.05261.669E-025.210E-042.402E-051.18312.964.790E-027.686E-063.861E+111.0524.710E-152.568E+033.941E-13651.06581.690E-025.275E-042.432E-051.18193.255.255E-028.326E-063.816E+111.0665.164E-152.817E+033.991E-13 (mmHg)atmatmatmatmgr/literLiter/detikgr/cm2detcm2/detatm2.028E-141.107E+041.945E-12

log Shlog ReLog Sc -14.58844138923.1492232597-12.421561908-14.44752799983.2896531929-12.4155471831-14.37060811943.3661861736-12.4099184697-14.3269662623.4096337344-12.4044062715-14.28700480153.4497894915-12.3989152931

perbandingan LAMINERLaju alir air = 0.3 ml/st wet baca delta hTin dryTout dryTwethumidity 12828257424.222222222282.482.47775.6228262474.422.444444444482.478.875.272.4328262375.622.611111111182.478.873.472.7

TRANSISILaju alir air = 3 ml/sdelta hTin dryTout dryTwethumidity 12827.52485.325.444444444482.481.575.277.822827.524.587.425.722222222282.481.576.178.332827248825.333333333382.480.675.277.6428272487.325.222222222282.480.675.277.452826.523.586.424.611111111182.479.774.376.3628262484.723.944444444482.478.875.275.1

TURBULENLaju alir air = 43.5 ml/sdelta hTin dryTout dryTwethumidity 126272494.926.277777777878.880.675.279.3226272595.826.388888888978.880.67779.532727259426.166666666780.680.67779.142727259225.888888888980.680.67778.6527272592.525.944444444480.680.67778.762727259526.277777777880.680.67779.3

laminer (2)KELOMPOK 2A : TIA, RAMOS, MKPENGOLAHAN DATA WETTED WALL COLUMNdengan data T in dan T wetfluida yang digunakan dalam manometer adalah Unknown fluid, dimana density-nya 0.766 gr/mL.1). laminer dengan Qair = 0.3 ml/detik dan humidity in = 45 % (kg uap air/kg udara kering)delta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAiTin dryTout dryTwetTbulkTint12827.624.22222222227227.8025.970.01880.01860.01960.029400.029090.0306382.481.6875.682.0478.74608920592252922.44444444447127.0024.650.01720.0180.01810.026960.028180.028297784.272.480.676.3737960845324.528.522.61111111117126.5024.500.01560.01650.01650.024520.025890.0258976.183.372.779.776.1074619104ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.01580.0165ERROR:#REF!0.024820.02589ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.01560.0169ERROR:#REF!0.024520.02651ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!0.01420.0148ERROR:#REF!0.022370.02329ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!

delta PPtPA0PALPAi udaraQudarav udaraGkGDABPBMShReSc750.71.000070.029400.029100.030641.173795052.00.03844.046E-062.227E+100.970201,586.597.097E-121501.41.000150.026970.028190.028291.1856135073.90.05526.667E-052.204E+100.97193.465E-102,277.487.099E-122252.01.000220.024520.025900.025901.18771850101.20.07582.484E-042.202E+100.97431.295E-093,126.477.095E-12ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!2250123.1ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!2550139.5ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!2750150.5ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!atmatm.gr. Liter...mL detik...cm det...gmol... det...gmol cm2.det.atmcm2/detatmERROR:#REF!ERROR:#REF!ERROR:#REF!

...gr.... cm.det2atmatmlog Shlog ReLog Sc-10.68054564493.2004644014-11.1489250895-9.46031957083.3574548004-11.1487971028-8.88779450963.4950538666-11.1490222742tekanan (kg/m.det2)rho (kg/m3)g (m/s2)h (m)h (mm)Cairan yang dipakai pada percobaan ini ERROR:#REF!ERROR:#REF!ERROR:#REF!Hg101292.8136009.80.76760bukanlah Hg atau Air, tapi cairan Unknown yangERROR:#REF!ERROR:#REF!ERROR:#REF!Air101292.810009.810.33610336density-nya sudah saya hitung sebesar 0.766 gr/mLERROR:#REF!ERROR:#REF!ERROR:#REF!Unknown101292.87669.813.493472584913493.5Anggap aja zat unknown ini sebagai zat A1 atm

diameter kolom = 4.825cmmasa jenis air =1gr/mllaju alir air =5ml/detviskositas air =0.01gr/cm.detRe Number air =2412.50--> Laminer


untuk Sc konstanUntuk Re konstan

perhitungan menggunakan kelima datauntuk Sc konstan:log Sh = a log Re + (log k + b log Sc).1yB1 x + A1Sh = k.Re-0.1938Sc-13.747A1 = 2.3099k = Sh/(Rea.Scb)B1 =-17.903ShReSckuntuk Re konstan:01586.588863002500log Sh = b log Sc + (log k + a log Re)20.00000000032277.481198348900 yB2 x + A20.00000000133126.467126090200A2 =156.18ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!B2 =1730ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!rata-rataERROR:#REF!ERROR:#REF!ERROR:#REF!ERROR:#REF!A1 - A2 = 153.8701 persamaan 2 dikurangi dengan persamaan 1 menjadi:b log Sc - a log Re = A1 - A2rupanya nilai k -nya ga bisa di carilog Sc = (a/b) log Re +166.31/b3hal ini karena komputernya ga sanggung menghitungIni karena nilai Sc yang kecil, sehingga kalau di pangkatkanhubungan antara Re dan Scakan sangat mendekati nol

untuk aliran transisi dan turbulen, metode perhitungannyamasih belum bener. Sebaiknya copy perhitungan aliranlaminer ini kemudian ganti angka-angkanya dengandata pada aliran transisi dan turbulen

penjelasan perhitungan data ada di file WORD:PENGOLAHAN DATA DAN PEMBAHASAN.Kalau ada yang bingung harap dipahami sendiri ya

-11.193maka b = -13.74700.0141maka a = -0.1938

a3=11.163-11.151b=0.00390.0017

transisi (2)PENGOLAHAN DATA WETTED WALL COLUMNdengan data T wet2). Transisi dengan Qair = 3 ml/sdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAiTin dryTout dryTwetTbulkTint12827.525.444444444485.327.7526.580.01720.01740.01760.026960.027270.0275282.481.577.881.9579.845006725922827.525.722222222287.427.7526.720.0180.01820.01830.028180.028490.0286682.481.578.381.9580.10192188243282725.33333333338827.5026.400.01720.01760.01740.026960.027570.0273382.480.677.681.579.52333188354282725.222222222287.327.5026.340.01720.01760.01750.026960.027570.0273682.480.677.481.579.42046298752826.524.611111111186.427.2525.910.01640.0170.01660.025740.026660.0261082.479.776.381.0578.6346891646282623.944444444484.727.0025.440.01720.0180.01740.026960.028180.0273082.478.875.180.677.7949671507

delta PPtPA0PALPAi udarav udaraQudaraGkGDABPBMShReSc750.68001.000070.026970.02730.027531.1736451.98289500.03841.442E-052.238E+100.97277.437E-111,586.477.064E-121501.36001.000150.028190.02850.028661.1736473.870213500.05462.698E-052.240E+100.97161.389E-102,254.467.057E-122252.04001.000220.026970.02760.027331.17364101.229618500.07491.423E-052.235E+100.97287.343E-113,089.447.075E-123002.72001.000300.026970.02760.027371.17364123.117122500.09112.795E-052.234E+100.97281.443E-103,757.437.078E-123753.40001.000370.025750.02670.026111.17364139.532725500.10322.108E-052.226E+100.97401.092E-104,258.427.103E-124504.08001.000440.026980.02820.027321.17364150.476427500.11135.043E-052.218E+100.97272.613E-104,592.427.130E-12...gr.... cm.det2atmatmatmatm.gr. Liter...cm det...mL detik...gmol... det...gmol cm2.det.atmcm2/detatm8.015E-101.954E+044.251E-11

log Shlog ReLog Sc-10.12862240023.2004322172-11.1509596622-9.85737006713.3530423804-11.1514100588-10.13410425613.4898803403-11.1502907564-9.84078123173.57489113-11.1500651749-9.96183599063.6292487923-11.1485544442-9.58278205033.6620413057-11.1469398164

diameter kolom = 4.8254.825masa jenis air =1gr/ml1laju alir air =12.92135ml/det12.4352331606viskositas air =0.01gr/cm.det0.01Re Number air =6234.55--> Transisi6000.00



log k + b log Sc = -12.352

B181.595A2899.85

log k + a log Re = 899.85

untuk Re dan Sc

Untuk Re konstan

b log Sc - a log Re = -912.202log Sc = (a/b) log Re + (A1-A2)/b-912.202/b -11.168--> b =81.7238846085a/b = 0.0051--> a = 0.4167918115

mencari harga k

Sh rata-rata = sigma Sh/n =1.603E-10

Re rata-rata = sigma Re/n =3.908E+03

Sc rata-rata = sigma Sc/n =8.501E-12

Sh = k.Re0.4168.Sc81.72

maka k = Sh/(Rea.Scb) = ERROR:#DIV/0!~0

dengan data Humidity alat

2). Transisi dengan Qair = 5.689 ml/detikdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAi1026.22624.186.526.1025.090.010.020.031.586E-023.122E-024.610E-022026.2262590.426.1025.550.010.020.031.586E-023.122E-024.610E-023025.425.22593.225.3025.150.010.020.031.586E-023.122E-024.610E-024025.2252594.225.1025.050.010.020.031.586E-023.122E-024.610E-025025.22524.895.925.1024.950.010.020.031.586E-023.122E-024.610E-02 (mmHg)0C0C0C%0C0C(kg uap air/kg udara kering)fraksi mol

delta hPtPA0PALPAiudaraQudaraGkGDABPBMShReSc151.01321.606E-025.015E-042.312E-051.18111.632.634E-024.390E-063.990E+111.0132.597E-151.412E+033.819E-13301.02631.627E-025.080E-042.342E-051.18112.253.635E-025.982E-063.953E+111.0263.578E-151.949E+033.855E-13451.03951.648E-025.145E-042.372E-051.18432.684.342E-027.054E-063.891E+111.0394.280E-152.328E+033.906E-13501.05261.669E-025.210E-042.402E-051.18512.964.799E-027.699E-063.840E+111.0524.733E-152.573E+033.956E-13601.06581.690E-025.275E-042.432E-051.18513.255.269E-028.348E-063.789E+111.0665.199E-152.825E+034.008E-13 (mmHg)atmatmatmatmgr/literLiter/detikgr/cm2detcm2/detatm2.039E-141.109E+041.954E-12

log Shlog ReLog Sc-14.58551012283.1498033826-12.4180284113 -14.44640682533.2897982964-12.413984528-14.36852270293.3669131481-12.40826868-14.32488092023.410361196-12.4027579518-14.28409443613.450952846-12.3970220332

turbulen (2)PENGOLAHAN DATA WETTED WALL COLUMNdengan data T wet3). Turbulen dengan Qair = 43.5 ml/detikdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAiTin dryTout dryTwetTbulkTint1262726.277777777894.926.5026.390.0180.01760.01820.028180.027570.0285578.880.679.379.779.49971929692262726.388888888995.826.5026.440.01970.01920.01910.030760.030010.0298578.880.679.579.779.59992997193272726.16666666679427.0026.580.01920.01920.01910.030010.030010.0298580.680.679.180.679.8460812484272725.88888888899227.0026.440.01920.01920.01910.030010.030010.0298580.680.678.680.679.59299637455272725.944444444492.527.0026.470.01920.01920.01910.030010.030010.0298580.680.678.780.679.64368593446272726.27777777789527.0026.640.01920.01920.01910.030010.030010.0298580.680.679.380.679.9470627688

delta PPtPA0PALPAi udarav udaraQudaraGkGDABPBMShReSc750.68001.00010.028180.027580.028561.181551.98289500.03871.795E-052.235E+100.97209.257E-111,597.087.027E-12konstanta yg digunakan:1501.36001.00010.030770.030010.029861.181573.870213500.05504.721E-052.236E+100.97022.430E-102,269.537.025E-12viskositas/miu = 0.018 cP = 1.8 E-04 gr/cm.det2252.04001.00020.030010.030010.029861.1776101.229618500.07510.000E+002.238E+100.97030.000E+003,099.747.041E-12cari lagi!dari psychrometric chart3002.72001.00030.030010.030010.029861.1776123.117122500.09140.000E+002.235E+100.97040.000E+003,769.957.050E-12dari percobaan3753.40001.00040.030020.030020.029861.1776139.532725500.10350.000E+002.236E+100.97040.000E+004,272.617.049E-12Sh perlu di cek lagi, yg disini pakai T int4504.08001.00040.030020.030020.029871.1776150.476427500.11170.000E+002.238E+100.97050.000E+004,607.727.040E-12...gr.... cm.det2atmatmatmatm.gr. Liter...cm det...mL detik...gmol... det...gmol cm2.det.atmcm2/detatm3.355E-101.962E+044.223E-11

log Shlog ReLog Sc-10.03354624843.2033260775-11.1532045872-9.6144494653.3559362407-11.1533607847

diameter kolom = 4.825cmmasa jenis air =1gr/mllaju alir air =25ml/detviskositas air =0.01gr/cm.detRe Number air =12062.50--> Turbulen



log k + b log Sc = -18.83

B1-2683.1A2-29935

log k + a log Re = -29935

untuk Re dan Sc

Untuk Re konstan

b log Sc - a log Re = 29916.17log Sc = (a/b) log Re + (A1-A2)/b29916/b = -11.15--> b =-2683.064573991a/b = -0.001--> a = 2.683064574

mencari harga k

Sh rata-rata = sigma Sh/n =1.678E-10

Re rata-rata = sigma Re/n =6.711E-11

Sc rata-rata = sigma Sc/n =3.923E+03

Sh = k.Re-0.001.Sc--2683

maka k = (Rea.Scb)/Sh = ERROR:#DIV/0!~0

dengan data alat humidity3). Turbulen dengan Qair = 36.259 ml/detikdelta hTin dryTout dryTwethumidity outTbulkTintHA0HALHIntYA0YALYAi10262726.194.426.5026.300.010.020.031.586E-023.122E-024.610E-022025.626.825.994.326.2026.050.010.020.031.586E-023.122E-024.610E-023024.826.825.995.825.8025.850.010.020.031.586E-023.122E-024.610E-024024.426.825.995.325.6025.750.010.020.031.586E-023.122E-024.610E-02502526.825.894.725.9025.850.010.020.031.586E-023.122E-024.610E-02 (mmHg)0C0C0C%0C0C(kg uap air/kg udara kering)fraksi molfraksi molfraksi mol

delta hPtPA0PALPAiQudaraGkGDABPBMShReSc151.01321.606E-025.015E-042.312E-051.17951.632.630E-024.384E-064.028E+111.0132.580E-151.410E+033.788E-13301.02631.627E-025.080E-042.342E-051.18072.253.634E-025.980E-063.969E+111.0263.568E-151.948E+033.841E-13451.03951.648E-025.145E-042.372E-051.18232.684.334E-027.042E-063.913E+111.0394.260E-152.324E+033.891E-13601.05261.669E-025.210E-042.402E-051.18312.964.790E-027.686E-063.861E+111.0524.710E-152.568E+033.941E-13651.06581.690E-025.275E-042.432E-051.18193.255.255E-028.326E-063.816E+111.0665.164E-152.817E+033.991E-13 (mmHg)atmatmatmatmgr/literLiter/detikgr/cm2detcm2/detatm2.028E-141.107E+041.945E-12

log Shlog ReLog Sc -14.58844138923.1492232597-12.421561908-14.44752799983.2896531929-12.4155471831-14.37060811943.3661861736-12.4099184697-14.3269662623.4096337344-12.4044062715-14.28700480153.4497894915-12.3989152931

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