Client InfoQuote #:ExampleDoc #:ExampleAssoc. RFQ #:ExampleVessel Tag #:Example4727 NW Evangeline ThruwayCust Name:ExampleCarencro, LA 70520Service:Example337.896.3815Relief Valve Body SizesRev: ABy: JJLChk: DBRAppr: MHDate: 6/20/2014vsAvailable OrificesFOR ESTIMATION PURPOSES ONLYOrifice Size1 X 21.5 X 21.5 X 2.51.5 X 32 X 32.5 X 43 X 44 X 66 X 86 X 108 X 10Inputs: Outputs:NominalDesignationArae (IN2)2.02.02.02.02.03.03.04.06.06.08.0Crude API30Inlet (L1)6inchPipesD0.110xxxBOPD3000PSV (L2)2inchE0.196xxxBWPD2000Gas Out (L3)3inchF0.307xxxMMSCFD10Oil Out (L4)3inchG0.503xxxOp.DesignWater Out (L5)2inchH0.785xxPres(psig)1100800N16inchNozzlesJ1.287xxxTemp. (F)100120N22inchK1.838xN33inchL2.853xxN43inchM3.600xN52inchN4.340xPSV"H"OrificeValvesP6.380xPCV51.41CvQ11.050xLCV-125.90CvR16.000xxLCV-218.45CvT26.000x

L1L2L3L4L5N1N2N3N4N5LCV-1(oil)LCV-2(water)PCV(gas)PSV(blocked flow)

Nozzles

2
stelios: stelios:Do Not Remove1Design Working Temperature (F)ERROR:#REF!2Operating Temperature - (F)100

11Minimum Operating Pressure (PSIG)20Design Working Pressure800PSI2Normal Operating Pressure (PSIG)125

NOZZLE SIZING CALCULATIONS11Designed Rates (MMSCFD-BPD)139.62Maximum Rates (MMSCFD-BPD)0.625INPUT DATAFluid Data (Including Surge)Gas (MMSCFD)Oil/Cond (BPD)Water (BPD)Total Fluid (BPD)Max Gas Case10.0300020005000Max Liquid Case10.0300020005000Gravities (Used both cases)0.650.881.00Total Liquid Gravities (MaxGas-MaxLiq)0.930.93

Operating ConditionsMax GasMax LiquidNote: Columns below set up for these two cases.Operating Pressure (PSIG)11001100Operating Temperature - (F)100100Compressibility F. (z) (MaxGas-MaxLiq)0.8550.855

INLET NOZZLEType of Inlet Feed DeviceInletMax Value - Dens. X Velocity^2 (LBS/FT-SEC^2)7500Mixture Density (LBS/FT3)14.1814.18Erosional Velocity (FT/SEC) 26.5626.56Gas Flowrate (FT3/SEC)1.691.69Gas Density (LBS/FT3)4.084.08Gas Mass Flowrate (LBS/SEC)6.886.882
stelios: stelios:Do not Remove Rounding factor2Actual Liquid Flowrate (FT3/SEC)0.390.39Total Liquid Mass Flowrate (LBS/SEC)22.5022.50Minimum Nozzle ID (INCHES)4.074.07SELECTED NOZZLENext Available Nozzle Size (INCHES)6.006.006.00Velocity of Mixture Thru Sel. Nozzle (FT/SEC)10.610.6Density of Mixture X Velocity ^2 (LB/FT-SEC^2)15851585

GAS OUTLET NOZZLEMax Value - Density X Velocity^2 (LBS/FT-SEC^2)50001
stelios: stelios:Do not Remove Rounding factor1Minimum Nozzle ID (INCHES)2.972.97SELECTED NOZZLENext Available Nozzle Size (INCHES)3.003.003.0Velocity of Gas thru Sel. Nozzle (FT/SEC)34.434.4Density of Gas X Velocity ^2 (LBS/FT-SEC^2)48194819

NOZZLE SIZING CALCULATIONS

OIL OUTLET NOZZLEMax Value - Line Velocity (FT/SEC)8Maximum Design Oil Rate (FT3/SEC)0.230.23Minimum Nozzle ID (INCHES)2.312.31SELECTED NOZZLENext Available Nozzle Size (INCHES)3.003.003.01
stelios: stelios:Do not Remove Rounding factor1Velocity of Oil thru Sel. Nozzle (FT/SEC)4.84.8

WATER OUTLET NOZZLEMax Value - Line Velocity (FT/SEC)8Maximum Design Water Rate (FT3/SEC)0.160.16Minimum Nozzle ID (INCHES)1.891.89SELECTED NOZZLENext Available Nozzle Size (INCHES)2.002.002.0Velocity of Water thru Sel. Nozzle (FT/SEC)7.17.1

RELIEF NOZZLE CALCULATIONSBLOCKED FLOW1
stelios: stelios:Do not Remove1Orifice Area for Gas (INCHES^2)0.35
A satisfied Microsoft Office user: =Qv*sqrt(T1*SG*z)/(1.175*c1*K*P1*Kb)whereQv=scfmT1=temp orSg=gas gravityz=compresssibility factorC1=coefficient =345 for natural gasK=coeffcient of discharge =0.975P1=inlet pressure = DWP+10%Kb=back pressure correction factor = 1.00.35Note: These calcs forOrifice Area for Liquid (INCHES^2)0.20
A satisfied Microsoft Office user: A=gpm*sqrt(SG)/(38*K*Kp*Kw*Kv*sqrt(1.25*P-Pb))wheregpm=rate in gals/minSg=liquid specific gravityK= coefficient of discharge =0.62Kp=capacity correction factor due to overpressureKw=factor due to backpressureKv=factor due to viscosityP=set pressurePb=backpressure,psig0.20preliminary screeing of MaxTotal Orifice Area Required (INCHES^2)0.554
A satisfied Microsoft Office user: This cell selects the offset for the "orifice"range. I've hidden it by changing the font color to white.nozzle sizes only.Orifice Selected/Actual Area(INCHES^2)"H"0.785REQUIRED NOZZLERequired Nozzle Size (INCHES)2.02.0

&F&APage &P of &N

&8Vessel Sizing Program, Copyright 2001 PetroDesigns, LLCAll Rights Reserved.&8Revision 0&8 &D

PSV_TableRelief Valve Body SizesvsAvailable OrificesOrifice Size1 X 21.5 X 21.5 X 2.51.5 X 32 X 32.5 X 43 X 44 X 66 X 86 X 108 X 10DesignationArae (IN2)2.02.02.02.02.03.03.04.06.06.08.0D0.110xxxE0.196xxxF0.307xxxG0.503xxxH0.785xxJ1.287xxxK1.838xL2.853xxM3.600xN4.340xP6.380xQ11.050xR16.000xxT26.000x

&F&APage &P of &N

&8Vessel Sizing Program, Copyright 2001 PetroDesigns, LLCAll Rights Reserved.&8Revision 0&8 &D

ConversionsMultiplybyto getInputsAcres435600Square FeetAcres 48400Square YardsAcre Feet435600Cubic FeetAcre Feet 3258510Gallons

Atmospheres 76.000Cms. of MercuryAtmospheres 29.920Inches of MercuryAtmospheres 33.900Feet of WaterAtmosphere14.700Lbs./sq. in.Barrels -- Oil42.000Gallons-- oil

Barrels Cem 376.000Lbs. -- CementBags/sacks cement 0.940Lbs. CemenBritish Thermal Units777.500Foot -- LbsBtu/min 12.960Ft. -- Lbs./secBtu/min0.020Horse PowerBtu/min17.570Watts

Cubic Feet1728.000Cubic InchesCubic Feet0.040Cubic YardsCubic Feet7.480GallonsCubic Feet/min0.120Gallons/see.Cubic Feet/rain 62.430Lbs. water/min.Cubic Feet/sec0.650Million Gals./Day

Cubic Feet/sec448.830Gallons/min.Feet12.000InchesFeet of water62.430Lbs./sq. ft.Feet of water0.430Lbs./sq. in.Feet/min 0.020Ft./sec.Feet/min0.010Miles/hr.

Feet/sec0.590Knots0Feet/sec0.680Miles/hr.Feet/sec0.010Miles/minGallons 0.130Cubic FeetGallons 231.000Cubic InchesGallons 8.000Pints (Liquid)

Gallons4.000Quarts ~ Liquid)Gallons Imperial1.200U. S. GallonsGallons Water8.350Lbs. WaterGallons/hour8.020Cubic Feet/hr.Horse Power42.440Btu/Min.Horse Power 33.000Foot-lbs./min.

Horse Power550.000Ft.-Lbs./Sec.Horse Power745.700WattsKilograms35.270OuncesKilograms2.200PoundsKilo Watts56.920Btu/min.Kilo Watts 1.340Horse PowerMiles 52800Feet

Miles1760.000YardsMiles/hr88.000Ft./Min.Miles/hr1.470Ft./sec.Milliliters0.030OuncesOunces0.060Lbs.Ounces (Fluid) 1.810Cubic Inches

Pounds453.590GramsPounds0.450KilogramsPounds16.000OuncesPounds0.000Tons (Short)Pounds Water0.020Cubic FeetPounds Water 27.680Cubic InchesPounds Water0.120GallonsPounds/sq ft 0.020Feet of Water0Pounds/sq in 2.310Feet of WaterQuarts (Dry)67.200Cubic InchesQuarts (Liquid)57.750Cubic InchesRadians 57.300DegreesRadians3438.000MinutesRadians0.640Quadrant0Square Feet 0.000AcresSquare Feet144.000Square InchesSquare miles 640.000AcresSquare yards9.000Square Feet0Temperature (C)+ 273 x 1273Abs. Temp. (K) (Kelvin)Temperature (C) +32 x 1.8 32Temp. (F)Temperature (F) +459.67 x 1459.67Abs. Temp. (R) (Rankine)Temperature (F) -32 x 5/9-17.78Temp.(C)

Tons Long 22400PoundsTons Short20000PoundsTons Short320000Ounces

Watts 0.060Btu/min.Watts44.260Foot-pounds/minWatt-Hours3.420BtuWatt-Hours26550Foot-poundsYards3.000FeetYards 36.000Inches

Yards 0.910Metersinch (in)0.250millimeter (mm)feet (ft)0.300meters mile (mi) 1.610kilometers square mile2.590square kilometer gallon per minute (gal/min) 0.060liters per second (L/s)

million gallons per day (Mgal/d) 0.040cubic meters per secondmillion gallons per day (Mgal/d) 37850cubic meter per dayfoot per second(ft/s) 0.310meter per secondcubic foot per second (ftS/s) 0.030cubic meter per secondfoot squared per second(ft~/s) 0.090meter squared per secondliter 10000cubic meterliter 1.060quartscubic centimeter 16.400Cubic inchcubic centimeter 0.030Ounces1 kilogram 2.210Poundspounds 453.600gramscm 0.390inch1 short ton of CO217.800McfCO2 @ 25 deg C and 1 atmteaspoons (tsp)5.000millilitersTablespoon (Tbsp)15.000millilitersjiggers1.500Ouncesjiggers44.400milliliters2000BWPD0.0358.34gpmcv18.4530APIn/a0.8761609907SG2000BWPD0.0000650.13ft^3/s3000BOPD0.0387.51gpmcv25.903000BOPD0.0000650.195ft^3/s10MMSCFD416666.666666667SCFH1100psig1114.7psia100deg F560Rankinex0.0089710236if x is greater than 0.702 the flow is chokedhttp://www.professionalgeologist.org/multiply_.htmY0.995728084cv51.41

Data SheetBrill-Beggs-Z.xlsDescription: This spreadsheet calculates gas compressibility factor based on Brill and Beggs correlation.Instruction: 1) Select a unit system; 2) Update data in the Input Data section; 3) Review result in the Solution section.Input Data: 10Pressure:1114.7 psia30 MPa1114.7 psiaTemperature:100 F100 C100 FGas specific gravity:0.65 air = 10.65air = 10.65 1 for airMole fraction of N2:0.020.10.02Mole fraction of CO2:0.0010.080.001Mole fraction of H2S:0.00070.020.0007

Solution:

Pseudocritical pressure =667 psia4.54 MPaPseudocritical temperature =369 R204.43 KPseudo-reduced pressure =1.671.67Pseudo-reduced temperature =1.521.52A =0.42820.4282B =0.62820.6282C =0.07390.0739D =0.97090.9709Gas compressibility factor z =0.85480.8548

Sheet1 (3)standard conditionsActual conditionpressure0psig14.7pressure1100psig1114.7temp60deg F520temp100deg F560Z std11Z act0.8548422310.854842231MMSCFD100ACFD1214031.58592473ACFH50584.6494135304ACFM843.0774902255ACFS14.0512915038