data Gate ValveLABORATORIUM HIDROLIKAFAKULTAS TEKNIK JURUSAN SIPILUNIVERSITAS MUSLIM INDONESIA>?TABEL PENGAMATAN PERCOBAAN F6 - A / B( ALIRAN PADA TATA PIPA )JENIS PERCOBAAN:GATE VALVENO. URT.VOLUMEWAKTUPEMBACAAN MANOMETERTEMP(Liter)(Dtk)Hg (mm)H2O (mm)(OC)14.008.003118.068.50278.309.6026624.008.603099.038.94279.379.9120934.0012.4430613.5312.222712.9413.0327144.0017.3430917.7818.122718.6618.60270Group:1Makassar,.. 20AsistenNoNamaStb.Laboratorium Hidrolika12345( )

perht Gate Valve1.6GATE VALVEDiketahui:Diameter pipa(d)=16.23mm=0.01623mLuas penampang(A)=.d2=0.000207m4Volume(v)=4.00ltr=0.004mTemperatur=27CGaya gravitasi=9.81m/dtPanjang Pipa(L)=1.80mKoef. Kehil. tng(K)=0.541.Menghitung Waktu Rata-Rata (tr)tr=t1 + t2 + t3 + t4 + t5n=8+8.06+8.5+8.3+9.65=8.492dtk2.Menghitung Debit Pengaliran (Q)Q=vtr=0.0048.492=0.000471m/dtk3.Menghitung Kecepatan Aliran (V)V=QA=0.0004710.00021=2.275362m/dtk4.Menghitung Bilangan Reynolds (Re)Re=r.V.dmSebelumnya! Nilai T diinterpolasi terlebih dulu, supaya diketahui nilai r dan m.T25=r=997.1kg/mm=0.000894kg/mdtkT30=r=995.7kg/mm=0.000801kg/mdtkT27=r=996.54kg/mm=0.000857kg/mdtkRe=996.54.2.275362.0.000210.00086=42942.065912>2800(Turbulen)5.Menghitung Koefisien Gesek (f)f=0.316.Re-0.25=0.316.42942.065912-0.25=0.0219526.Menghitung Kehilangan Energi (hl hitung)hlht=K .V2g=0.54.2.27536222.9.81=0.142494m7.Menghitung Beda Tinggi (hl ukur)hluk=(Hgmax - Hgmin).(gHg - gH2O)1000=311-266.13.6-1.01000=0.567m8.Perhitungan TabelNo.trQVRefhlhthluk(dtk)(m/dtk)(m/dtk)(m)(m)1.8.4920.0004712.27536242942.065910.0014900.1424940.567002.9.170.0004362.1062839751.043830.0016100.1221031.260003.12.8320.0003121.50724628445.696590.0022500.0625260.441004.18.10.0002211.06763320149.042950.0031760.0313720.491409.Tabel Perhitungan Persamaan Last QuartsNo.hl hitung (x)hl ukur (y)xyx(m)(m)(m)(m)1.0.1424940.5670.0807940.0203052.0.1221031.260.153850.0149093.0.0625260.4410.0275740.003914.0.0313720.49140.0154160.000984S0.3584952.75940.2776340.040108Rumus persamaan grafik liniery = A - B . xB=n . xy - x . yn . x - (x)=4.0.277634-0.358495.2.75944.0.040108-0.128519=3.801112A=y - B . xn=2.7594-3.80111.0.3584954=0.34918Jika y = A + B . x, makaNoxy100.349180214.150292327.9514044311.7525165415.5536286519.354740

data VenturiLABORATORIUM HIDROLIKAFAKULTAS TEKNIK JURUSAN SIPILUNIVERSITAS MUSLIM INDONESIATABEL PENGAMATAN PERCOBAAN F6 - A / B( ALIRAN PADA TATA PIPA )JENIS PERCOBAAN:VENTURI METERNO. URT.VOLUMEWAKTUPEMBACAAN MANOMETERTEMP(Liter)(Dtk)Hg (mm)H2O (mm)(OC)14.008.363112148.278.96278.778.7427363924.009.163141869.099.442710.0410.1126464434.0011.9230819511.4811.812711.4311.7426964144.0014.9031015414.6114.902714.8114.31267640Group:1Makassar,.. 20AsistenNoNamaStb.Laboratorium Hidrolika12345( )

perht Venturi1.7VENTURI METERDiketahui:Diameter pipa(d1)=21.85mm=0.02185mDiameter pipa(d2)=16.23mm=0.01623mLuas penampang(A1)=.d2=0.000375m4Luas penampang(A2)=.d2=0.000207m4Volume(v)=4.00ltr=0.004mTemperatur=27CGaya gravitasi=9.81m/dt1.Menghitung Waktu Rata-Rata (tr)tr=t1 + t2 + t3 + t4 + t5n=8.36+8.27+8.96+8.77+8.745=8.62dtk2.Menghitung Debit Pengaliran (Q)Q=vtr=0.0048.62=0.000464m/dtk3.Menghitung Kecepatan Aliran (V)V1=QV2=QA1A2=0.000464=0.0004640.0003750.000207=1.237333m/dtk=2.241546m/dtk4.Menghitung Bilangan Reynolds (Re)Re=r.V.dmSebelumnya! Nilai T diinterpolasi terlebih dulu, supaya diketahui nilai r dan m.T25=r=997.1kg/mm=0.000894kg/mdtkT30=r=995.7kg/mm=0.000801kg/mdtkT27=r=996.54kg/mm=0.000857kg/mdtkRe=996.54.1.237333.0.000380.00086=31437.785808>2800(Turbulen)5.Menghitung Koefisien Gesek (f)f=0.316.Re-0.25=0.316.31437.785808-0.25=0.0237316.Menghitung Beda Tinggi (hl ukur)hluk=(Hgmax - Hgmin).(gHg - gH2O)1000=311-266.13.6-1.01000=0.567m7.Perhitungan Koefisien Pengaliran (Cd)Cd=Q(A1(1 - (A1/A2)) . 2gH0.000464=0.0004640.000375.1-0.0003752-.2.9.81.0.56700.000207=0.0000028.Perhitungan TabelNo.trQVRefhlukCd(dtk)(m/dtk)V1 (m/dt)V2 (m/dt)(m)1.8.620.0004641.2373332.24154631437.7858080.0237310.47880.0000022.9.5680.0004181.1146672.01932428321.1248660.0243590.630.0000023.11.6760.0003430.9146671.65700523239.5848430.0255940.49140.0000024.14.7060.0002720.7253331.31401018429.0433490.0271210.54180.000001

data OrificeLABORATORIUM HIDROLIKAFAKULTAS TEKNIK JURUSAN SIPILUNIVERSITAS MUSLIM INDONESIATABEL PENGAMATAN PERCOBAAN F6 - A / B( ALIRAN PADA TATA PIPA )JENIS PERCOBAAN:ORIFICENO. URT.VOLUMEWAKTUPEMBACAAN MANOMETERTEMP(Liter)(Dtk)Hg (mm)H2O (mm)(OC)14.008.363112148.278.96278.778.7427363924.009.163141869.099.442710.0410.1126464434.0011.9230819511.4811.812711.4311.7426964144.0014.9031019414.6114.902714.8114.31267640Group:1Makassar,.. 20AsistenNoNamaStb.Laboratorium Hidrolika12345( )

perht Orifice1.8ORIFICEDiketahui:Diameter pipa(d1)=25.32mm=0.02532mDiameter pipa(d2)=21.85mm=0.02185mLuas penampang(A1)=.d2=0.000504m4Luas penampang(A2)=.d2=0.000375m4Volume(v)=4.00ltr=0.004mTemperatur=27CGaya gravitasi=9.81m/dtPanjang Pipa(L)=1.00m1.Menghitung Waktu Rata-Rata (tr)tr=t1 + t2 + t3 + t4 + t5n=8.36+8.27+8.96+8.77+8.745=8.62dtk2.Menghitung Debit Pengaliran (Q)Q=vtr=0.0048.62=0.000464m/dtk3.Menghitung Kecepatan Aliran (V)V1=QV2=QA1A2=0.000464=0.0004640.0005040.000375=0.920635m/dtk=1.237333m/dtk4.Menghitung Bilangan Reynolds (Re)Re=r.V.dmSebelumnya! Nilai T diinterpolasi terlebih dulu, supaya diketahui nilai r dan m.T25=r=997.1kg/mm=0.000894kg/mdtkT30=r=995.7kg/mm=0.000801kg/mdtkT27=r=996.54kg/mm=0.000857kg/mdtkRe=996.54.0.920635.0.000500.00086=27105.978933>2800(Turbulen)5.Menghitung Koefisien Gesek (f)f=0.316.Re-0.25=0.316.27105.978933-0.25=0.0246286.Menghitung Beda Tinggi (hl ukur)hluk=(Hgmax - Hgmin).(gHg - gH2O)1000=311-273.13.6-1.01000=0.4788m7.Perhitungan Koefisien Pengaliran (Cd)Cd=Q(A1(1 - (A1/A2)) . 2gH0.000464=0.0004640.000504.1-0.0005042-.2.9.81.0.47880.000375=0.0000018.Perhitungan TabelNo.trQV(Re)fhlhtCd(dtk)(m/dtk)V1(m/dt)V2(m/dt)(m)1.8.620.0004640.9206351.23733328976.5832010.0242200.47880.0000012.9.5680.0004180.8293651.11466726103.8999450.0248610.630.0000013.11.6760.0003430.6805560.91466721420.2018790.0261200.49140.0000014.14.7060.0002720.5396830.72533316986.2859350.0276800.54180.000001

data Globe valveLABORATORIUM HIDROLIKAFAKULTAS TEKNIK JURUSAN SIPILUNIVERSITAS MUSLIM INDONESIATABEL PENGAMATAN PERCOBAAN F6 - A / B( ALIRAN PADA TATA PIPA )JENIS PERCOBAAN:GLOBE VALVENO. URT.VOLUMEWAKTUPEMBACAAN MANOMETERTEMP(Liter)(Dtk)Hg (mm)H2O (mm)(OC)14.008.503004558.668.22278.448.7227845924.009.163064349.049.09279.359.2527243934.0011.4730540312.5612.842712.8713.2727341244.0019.3430839018.9419.602719.6119.88270398Group:1Makassar,.. 20AsistenNoNamaStb.Laboratorium Hidrolika12345( )

perht Globe Valve1.9GLOBE VALVEDiketahui:Diameter pipa(d)=16.23mm=0.01623mLuas penampang(A)=.d2=0.000207m4Volume(v)=4.00ltr=0.004mTemperatur=27CGaya gravitasi=9.81m/dtKoef. Kehil. tng(K)=1.001.Menghitung Waktu Rata-Rata (tr)tr=t1 + t2 + t3 + t4 + t5n=8.5+8.66+8.2+8.44+8.725=8.508dtk2.Menghitung Debit Pengaliran (Q)Q=vtr=0.0048.508=0.000470m/dtk3.Menghitung Kecepatan Aliran (V)V=QA=0.000470.00021=2.270531m/dtk4.Menghitung Bilangan Reynolds (Re)Re=r.V.dmSebelumnya! Nilai T diinterpolasi terlebih dulu, supaya diketahui nilai r dan m.T25=r=997.1kg/mm=0.000894kg/mdtkT30=r=995.7kg/mm=0.000801kg/mdtkT27=r=996.54kg/mm=0.000857kg/mdtkRe=996.54.2.270531.0.000210.00086=42850.892235>2800(Turbulen)5.Menghitung Koefisien Gesek (f)f=0.316.Re-0.25=0.316.42850.892235-0.25=0.0219636.Menghitung Kehilangan Energi (hl hitung)hlht=K .V2g=1.00.2.27053122.9.81=0.262758m7.Menghitung Beda Tinggi (hl ukur)hluk=(Hgmax - Hgmin).gH2O1000=300-278.1.01000=0.022m8.Perhitungan TabelNo.trQVRefhlhthluk(dtk)(m/dtk)(m/dtk)(m)(m)1.8.5080.000472.27053142850.8922350.0219630.2627580.27722.9.1780.0004362.10628039751.0438290.0223790.2261170.42843.12.6020.0003171.53140128901.5649730.0242360.1195310.40324.19.4740.0002050.99033818690.2829840.0270260.0499880.47889.Tabel Perhitungan Persamaan Last QuartsNo.hl hitung (x)hl ukur (y)xyx(m)(m)(m)(m)1.0.2627580.27720.0728370.0690422.0.2261170.42840.0968690.0511293.0.1195310.40320.0481950.0142884.0.0499880.47880.0239340.002499S0.6583941.58760.2418350.136958Rumus persamaan grafik liniery = A - B . xB=n . xy - x . yn . x - (x)=4.0.241835-0.658394.1.58764.0.136958-0.433483=-0.681478A=y - B . xn=1.58760--0.681478.0.6583944=0.50907Jika y = A + B . x, makaNoxy100.50907021-0.17240832-0.85388643-1.53536454-2.21684265-2.898320

data Tikungan 90LABORATORIUM HIDROLIKAFAKULTAS TEKNIK JURUSAN SIPILUNIVERSITAS MUSLIM INDONESIATABEL PENGAMATAN PERCOBAAN F6 - A / B( ALIRAN PADA TATA PIPA )JENIS PERCOBAAN:TIKUNGAN 90NO. URT.VOLUMEWAKTUPEMBACAAN MANOMETERTEMP(Liter)(Dtk)Hg (mm)H2O (mm)(OC)14.008.503004558.668.22278.448.7227845924.009.163064349.049.09279.359.2527243934.0011.4730540312.5612.842712.8713.2727341244.0019.3430839018.9419.602719.6119.88270398Group:1Makassar,.. 20AsistenNoNamaStb.Laboratorium Hidrolika12345( )

perht Tikungan 901.10TIKUNGAN 90Diketahui:Diameter pipa(d)=16.23mm=0.01623mLuas penampang(A)=.d2=0.000207m4Volume(v)=4.00ltr=0.004mTemperatur=27CGaya gravitasi=9.81m/dtKoef. Kehil. tng(K)=0.901.Menghitung Waktu Rata-Rata (tr)tr=t1 + t2 + t3 + t4 + t5n=8.5+8.66+8.2+8.44+8.725=8.508dtk2.Menghitung Debit Pengaliran (Q)Q=vtr=0.0048.508=0.000470m/dtk3.Menghitung Kecepatan Aliran (V)V=QA=0.000470.00021=2.270531m/dtk4.Menghitung Bilangan Reynolds (Re)Re=r.V.dmSebelumnya! Nilai T diinterpolasi terlebih dulu, supaya diketahui nilai r dan m.T25=r=997.1kg/mm=0.000894kg/mdtkT30=r=995.7kg/mm=0.000801kg/mdtkT27=r=996.54kg/mm=0.000857kg/mdtkRe=996.54.2.270531.0.000210.00086=42850.892235>2800(Turbulen)5.Menghitung Koefisien Gesek (f)f=0.316.Re-0.25=0.316.42850.892235-0.25=0.0219636.Menghitung Kehilangan Energi (hl hitung)hlht=K .V2g=0.90.2.27053122.9.81=0.236482m7.Menghitung Beda Tinggi (hl ukur)hluk=(Hgmax - Hgmin).(gHg - gH2O)1000=300-278.13.6-1.01000=0.2772m8.Perhitungan TabelNo.trQVRefhlhthluk(dtk)(m/dtk)(m/dtk)(m)(m)1.8.5080.000472.27053142850.892230.0014940.2364820.27722.9.1780.0004362.10628039751.043830.0016100.2035050.42843.12.6020.0003171.53140128901.564970.0022140.1075770.40324.19.4740.0002050.99033818690.282980.0034240.0449890.47889.Tabel Perhitungan Persamaan Last QuartsNo.hl hitung (x)hl ukur (y)xyx(m)(m)(m)(m)1.0.2364820.27720.0655530.0559242.0.2035050.42840.0871820.0414143.0.1075770.40320.0433750.0115734.0.0449890.47880.0215410.002024S0.5925531.58760.2176510.110935Rumus persamaan grafik liniery = A - B . xB=n . xy - x . yn . x - (x)=4.0.217651-0.592553.1.58764.0.110935-0.351119=-0.757206A=y - B . xn=1.58760--0.757206.0.5925534=0.509071Jika y = A + B . x, makaNoxy100.50907121-0.24813532-1.00534143-1.76254754-2.51975365-3.276959