Customer Input Values

Version 1.13 Beta Do Not Change

Review

CUSTOMER:

PROJECT:

DATE: 5/8/2023

TAG NUMBER:

Input Values Suggested Valve Sizing Manual InputMedia UNITS Valve Model

Inlet Pressure 100 Valve Size 2 1/2 Inches 2 1/2

Min Flow Rate 150 Valve CV 137 137

Max Flow Rate 150 DP at Min Flow in PSI 1.20 PSI 1.20

Temperature 100 DP at Max Flow in PSI 1.20 PSI 1.20

Specific Gravity 1.00

Vapor Pressure 100

Line size Inches 3

Pipe Schedule Line Velocity at Min Flow 11.2 FT/S

Pipe Material LineVelocity at Max Flow 11.2 FT/S

Installation requirements;1- Insure a minimum of 5 straight diameters upstream and 3 downstream the valve2- This sizing is based on largest full open valve size for the minimum flow

Valve Internal Spring customer Input Values

Version 1.14 Beta Do Not Change

Check Valve or line size

CUSTOMER:

PROJECT:

DATE: 5/8/2023

TAG NUMBER:

INPUT VALUES Suggested Maximum Valve Size Manual InputMedia UNITS Valve Model

Inlet Pressure 1.30 Valve Size #N/A Inch 1.5

Min Flow Rate 30.00 SCFH Valve CV #N/A 38

Max Flow Rate 30.00 SCFH DP at Min Flow #N/A PSI 0.01

Temperature 150.0 DP at Max Flow #N/A PSI 0.01

Media Other

Specific Gravity 1.305 2

Mol weight 32 29

Ratio Specific heat 1.4 1.4

Line size 1.5 Line Velocity at Min Flow 15.10 FT/S

Pipe Schedule LineVelocity at Max Flow 15.10 FT/S

Pipe Material Mach # 0.01

Installation requirements;1- Insure a minimum of 5 straight diameters upstream and 3 downstream of the valve2- The suggested sizing is based on largest full open valve size for the minimum flow, use manual input to select smaller size

Err:502#N/A

Liquid CalculationsVALVE ACCEPTABLE SIZE CV

0 48 479140 42 449830 36 256750 30 180410 24 101050 20 77690 18 57990 16 39110 14 32260 12 32060 10 26230 8 14400 6 9310 5 6790 4 3810 3 2211 2.5 1371 2 861 1.5 38

2.5 2137 21.202.5

1 3Schedule

104080

Material 1Stainless SteelCarbon SteelFRPPVC

Gas

VALVE ACCEPTABLE VALVE ACCEPTABLE LIGHT VALVE ACCEPTABLE LS

0 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 0

#N/A #N/A #N/A#N/A #N/A #N/A#N/A #N/A #N/A1 1/2

1 1.61 0.994019550549895

Schedule 2

MaterialStainless Steel 2Carbon SteelFRPPVC

Gas Units Inputs

6 3pressure PSIA 33.55 Min Flow SCFH

PSIA 1.30 CFHKPA 0.19 CFM

18.49 Kg/HrBar Abs 18.85 Lb/hr

PSIG 16.00 Lb/SecBar G 33.55

SCFHSCFM

Checksum

Min Flow in CFHFor Mach Calculation

Vapor Pressure portion PDry air pressure portion PTemp in CActual Density correction for RHActual Asssumed Dry DensityCorrection factor for SG of moist air

Liquid Unit Input3 pressure PSIA 8

From 1422.33 FromBar A 1450.37 Kg/HrBar G 1464.87 Lb/hrKPA 14.50 LPM

1422.33 LPSPSIA 100.00

kg/cm2

NM3/hrNM3/sec

M3/hrM3/sec

kg/cm2

M3/D

PSIG 114.70N/A N/AN/A N/A USGPMN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/AN/A N/A N/A

M3/hrM3/sec

Liquid CalculationsDP FULL OPEN DP of valve AT Index

0.36 9.80071276E-06 1 1 1/20.25 1.111951093E-05 2 2 0.19 3.41319903E-05 3 2 1/20.41 6.912916404E-05 4 3 0.17 0.0002203483904 5 4 0.26 0.0003727797178 6 5 0.26 0.0006690773076 7 6 0.13 0.0014709804006 8 8 0.15 0.0021619905534 9 10 0.14 0.0021890489954 10 12 0.12 0.0032702875193 11 14 0.14 0.0108506944444 12 16 0.25 0.0259587129555 13 18 0.34 0.0488026010702 14 20 0.21 0.1550003100006 15 24

0.8 0.4606785282857 16 30 0.37 1.198785230966 17 36 0.36 3.0421849648459 18 42 2.39 15.581717451524 19 48

SIZE CV DP FULL OPEN DP FULL OPEN LIGHT

48 47914 0.227772 0.39860142 44983 0.158175 0.028471536 25675 0.120213 0.066433530 18041 0.259407 0.085414524 10105 0.107559 0.05694320 7769 0.164502 0.066433518 5799 0.164502 0.05694316 3911 0.082251 0.03796214 3226 0.094905 0.047452512 3206 0.11 0.0710 2623 0.08 0.058 1440 0.11 0.066 931 0.2 0.055 679 0.19 0.054 381 0.14 0.083 221 0.31 0.08

2.5 137 0.16 0.052 86 0.22 0.17

1.5 38 1.512153 1.1271

With SA or Choked 45 deg.Light StandardWithout 1

3 2

gas v=3.057*Q/d^2v=ft/s Q=cfm d=in

Mach Number for gas = Qa /( 5574 * Av * sqrt( k * T / Mw )Qa = Flow Rate in cfhAv = Port Area in2k = Ratio of specific heats k= cp/cvT = RenkinMw = molecular weight of gas

Gas Units Inputs

3 1795.18 Max Flow SCFH 795.18

31.05 CFH 31.051862.91 CFM 1862.91795.18 Kg/Hr 795.18361.01 Lb/hr 361.01

1299638.99 Lb/Sec 1299638.991119.03 1119.03

0.31 0.311108.87 1108.87

3991947.91 3991947.9130.00 SCFH 30.00

1800.00 SCFM 1800.00

5299490.45 5299490.45

768.33 Max Flow in CFH 768.33For Mach Calculation

15477406.0085085-15246086.9111585

337.52-32.0557143900248 KG/M31.31961533125741

-24.2917110999916

0.03

Liquid Unit InputMin flow USGPM 8 Max Flow USGPM 1

150 From 150 From0.66045 Kg/Hr 0.66045

0.29952380952381 Lb/hr 0.2995238095238139.600 LPM 39.600

2377.500 LPS 2377.500 N/A15850.800 15850.800 N/A

Temp in oRoFoCoR

NM3/hrNM3/sec

M3/hrM3/sec

oFoCoR

M3/D

660.450 660.450 N/A2377548.450 2377548.450 N/A

150.000 USGPM 150.000 N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/A

M3/hrM3/sec

Valve Data

CV SA CV Port Area sqr in38 0.994

34 86 1.48554 137 2.185

101 221 3.746168 381 6.633277 679 11.293450 931 16.117922 1440 29.340

1395 2623 44.9242073 3206 63.6171581 3226 83.5651916 3911 122.3322842 5799 132.5723807 7769 168.4644951 10105 213.7238840 18041 345.841

12581 25675 370.93722042 44983 480.11123478 47914 842.692

DP FULL OPEN LS DP of valve AT MIN PROCESS FLOW

0.2016 3.5371270109833E-090.0144 4.01308796943458E-090.0336 1.23184086502511E-080.0432 2.4949066394799E-080.0288 7.95248532006628E-080.0336 1.34538093428144E-070.0288 2.41473398431707E-070.0192 5.30884297408062E-07

0.024 7.80273371050064E-070.06 7.90038900207601E-070.03 1.180263374901E-060.03 3.91607073364883E-060.04 9.36863134508153E-060.04 1.76131065855189E-050.04 5.5940399096825E-050.03 0.0001662612205584290.02 0.000432647678261720.02 0.00109794000450165

0.265734 0.00562352096488519

Mach Number for gas = Qa /( 5574 * Av * sqrt( k * T / Mw )

Gas Units Inputs

610.67610.67761.67150.00

Liquid Unit Input1

1019.36 From559.67 PSIA671.67 KPA100.00

N/A Bar AN/A PSIG

Temp in oR

kg/cm2

N/A Bar GN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/A

Valve DataPipe ID

Sched 10 Sched 40Stainless Steel Carbon Steel FRP PVC StainlesCarbon Steel FRP

1.682 1.682 N/A N/A 1.61 1.61 1.612.157 2.157 N/A N/A 2.067 2.067 2.0672.635 2.635 N/A N/A 2.469 2.469 2.469

3.26 3.26 N/A N/A 3.068 3.068 3.0684.26 4.26 N/A N/A 4.026 4.026 4.026

5.295 5.295 N/A N/A 5.047 5.047 5.0476.357 6.357 N/A N/A 6.065 6.065 6.0658.329 8.329 N/A N/A 7.981 7.981 7.98110.42 10.42 N/A N/A 10.02 10.02 10.0212.39 12.39 N/A N/A 12 11.938 11.938

13.5 13.5 N/A N/A 13.124 13.124 13.12415.5 15.5 N/A N/A 15 15 1517.5 17.5 N/A N/A 16.876 16.876 16.87619.5 19.5 N/A N/A 18.812 18.812 18.81223.5 23.5 N/A N/A 22.624 22.624 22.624

29.376 29.376 N/A N/A 29.25 29.25 N/A35.376 35.376 N/A N/A 35.25 35.25 N/A

N/A N/A N/A N/A 41.25 41.25 N/AN/A N/A N/A N/A 47.25 47.25 N/A

h

1849600

1

Gas Properties

Gas Mw Density Sg R kSelected gas 16 32 0.0831 1.305 48.3 1.4

1 Other 1.305 0.1504 2 1.42 Acetylene 26 0.0682 0.9070 59.4 1.33 Air 29 0.0752 1.0000 53.3 1.44 Amonia 17 0.0448 0.5960 91 1.325 Argon 39.9 0.1037 1.3790 38.7 1.676 Butane 58.1 0.1554 2.0670 26.5 1.117 Carbon Dioxide 44 0.1150 1.5290 35.1 1.38 Chlorine 70.9 0.1869 2.4860 21.8 1.339 Ethane 30 0.0789 1.0490 51.5 1.22

10 Ethylene 28 0.0733 0.9750 55.1 1.2211 Hydrogen Chlori 36.5 0.0954 1.2680 42.4 1.4112 Hydrogen 2 0.0052 0.0695 766.8 1.4113 Methane 16 0.0417 0.5540 96.4 1.3214 Natural Gas 19.5 0.0502 0.6670 79.1 1.2715 Nitrogen 28 0.0727 0.9670 55.2 1.4116 Oxygen 32 0.0831 1.3050 48.3 1.417 Propane 44.1 0.1175 1.5620 35 1.1518 Propylene 42.1 0.1091 1.4510 36.8 1.1419 Sulphur Dioxyde 64.1 0.1703 2.2640 24 1.2620 EtOH N/A 0.028 0.3723 N/A N/A21 INRU feed 49.7856 0.153 2.0346 N/A N/A22 Unknown N/A 0.0497 1.1092 N/A N/A23 N/A N/A N/A N/A N/A N/A24 N/A N/A N/A N/A N/A N/A25 N/A N/A N/A N/A N/A N/A26 N/A N/A N/A N/A N/A N/A27 N/A N/A N/A N/A N/A N/A28 N/A N/A N/A N/A N/A N/A29 N/A N/A N/A N/A N/A N/A30 N/A N/A N/A N/A N/A N/A31 N/A N/A N/A N/A N/A N/A32 N/A N/A N/A N/A N/A N/A33 N/A N/A N/A N/A N/A N/A34 N/A N/A N/A N/A N/A N/A35 N/A N/A N/A N/A N/A N/A

Liquid Unit Input Liquid PropertiesVapor P. PSIA Liquid

100.00 Selected Liquid 2100.00 1 Other

14.50 2 Water1422.33 3 Alcool Met.1450.37 4 Chlorine

114.50 5 Citric Acid

1464.87 6 Ferric Chloride N/A 7 GasolineN/A 8 GlycolN/A 9 KeroseneN/A 10 Nitric AcidN/A 11 Oil VegetableN/A 12 Phosphoric AcidN/A 13 Sodium ChlorideN/A 14 Sodium HydroxidN/A 15 Sodium SulfateN/A 16 StarchN/A 17 Sulfuric AcidN/A 18 N/A

19 N/A20 N/A21 N/A22 N/A23 N/A24 N/A25 N/A26 N/A27 N/A28 N/A29 N/A30 N/A31 N/A32 N/A33 N/A34 N/A35 N/A

Valve DataPipe ID

Sched 40 Sched 80PVC Stainle Carbon Steel FRP PVC DP FULL DP FULL DP FULL OPEN L

45 Standard 451.61 1.5 1.5 1.5 1.5 1.51215 2.39 1.1271

2.069 1.939 1.939 1.939 1.939 0.22 0.36 0.172.469 2.323 2.323 2.323 2.323 0.16 0.37 0.053.068 2.9 2.9 2.9 2.9 0.31 0.8 0.083.998 3.826 3.826 3.826 3.786 0.14 0.21 0.085.047 4.813 4.813 4.813 4.813 0.19 0.34 0.056.031 5.761 5.761 5.761 5.709 0.2 0.25 0.057.943 7.625 7.625 7.625 7.565 0.11 0.14 0.069.976 9.75 9.562 9.562 9.492 0.08 0.12 0.0511.89 11.75 11.374 11.374 11.294 0.11 0.14 0.07

13.072 12.5 12.5 12.5 12.41 0.09 0.15 0.0514.94 14.31 14.312 14.312 14.214 0.08 0.13 0.04

16.808 16.12 16.124 16.124 16.014 0.16 0.26 0.0618.863 17.94 17.938 17.938 17.614 0.16 0.26 0.07

22.54 21.56 21.562 21.562 21.418 0.11 0.17 0.06N/A 29 29 N/A N/A 0.26 0.41 0.09N/A 35 35 N/A N/A 0.12 0.19 0.07N/A 41 41 N/A N/A 0.16 0.25 0.03N/A 47 47 N/A N/A 0.23 0.36 0.40

Vapor P. PSIA Sg14.7 1

14.7 1N/A 0.796N/A 1.42N/A 1.54

N/A 1.23N/A 0.862N/A 1.11N/A 0.825N/A 1.5N/A 0.92N/A 1.83N/A 1.19N/A 1.27N/A 1.24N/A 1.5N/A 1.83N/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/A

Valve Data

DP FULL OPEN LDP FULL OPEN LS DP FULL OPEN LSStandard 45 Standard

1.7368 0.265734 0.42 00.26 0.02 0.03 0.3953488372093020.18 0.02 0.1 0.394160583941606

0.2 0.03 0.09 0.4570135746606330.17 0.04 0.08 0.4409448818897640.13 0.04 0.1 0.4079528718703980.09 0.04 0.08 0.4833512352309350.08 0.03 0.05 0.6402777777777780.08 0.03 0.06 0.53183377811666

0.1 0.06 0.09 0.6466001247660640.075 0.02 0.05 0.488609296162571

0.06 0.02 0.040.09 0.03 0.06

0.105 0.03 0.070.09 0.03 0.06

0.135 0.04 0.090.105 0.03 0.070.045 0.01 0.03

0.63 0.20 0.42