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Liquid Flow

Pressure Drop for CPA 50E Flow Conditioners

(edit the values in Blue)









CPA 50E Pressure Loss Coefficient K = 1.6



Tube Bundle K= 0.75

Nominal Liquid Specific Pressure Pressure Liquid

Pipe Size Flow Gravity Loss Loss Flow Rate Pipe Area Velocity Velocity Dp Dp

[in.] [GPM] [S.G.] [PSI] [mbar] in³/min in² Ft/sec. m/sec pascals PSI



2 225 1.00000 5.69 392.40 866 3.14 22.978 7.004 39240.27 5.691

3 225 1.00000 1.12 77.51 866 7.07 10.212 3.113 7751.16 1.124

4 225 1.00000 0.36 24.53 866 12.57 5.744 1.751 2452.52 0.356

6 225 1.00000 0.07 4.84 866 28.27 2.553 0.778 484.45 0.070

8 225 1.00000 0.02 1.53 866 50.27 1.436 0.438 153.28 0.022

10 225 1.00000 0.01 0.63 866 78.54 0.919 0.280 62.78 0.009

12 225 1.00000 0.00 0.30 866 113.10 0.638 0.195 30.28 0.004

14 225 1.00000 0.00 0.16 866 153.94 0.469 0.143 16.34 0.002

16 225 1.00000 0.00 0.10 866 201.06 0.359 0.109 9.58 0.001

18 225 1.00000 0.00 0.06 866 254.47 0.284 0.086 5.98 0.001

20 225 1.00000 0.00 0.04 866 314.16 0.230 0.070 3.92 0.001

22 225 1.00000 0.00 0.03 866 380.13 0.190 0.058 2.68 0.000

24 225 1.00000 0.00 0.02 866 452.39 0.160 0.049 1.89 0.000

26 225 1.00000 0.00 0.01 866 530.93 0.136 0.041 1.37 0.000

28 225 1.00000 0.00 0.01 866 615.75 0.117 0.036 1.02 0.000

30 225 1.00000 0.00 0.01 866 706.86 0.102 0.031 0.78 0.000

36 225 1.00000 0.00 0.00 866 1017.88 0.071 0.022 0.37 0.000

42 225 1.00000 0.00 0.00 866 1385.44 0.052 0.016 0.20 0.000

Pressure Drop for CPA 50E Flow Conditioners

(edit the values in Blue)









CPA 50E Pressure Loss Coefficient K = 1.6



Tube Bundle K= 0.75



Nominal Gas Compressibility Specific Line Temperature Pressure

Pipe Size Flow Factor Gravity Pressure Flowing Loss

[in.] [SCFH] [Zf] [S.G.] [PSIA] [°F] [PSI]



2 4000000 0.810000 0.600 1414.73 60 173.40

3 4000000 0.810000 0.600 1414.73 60 34.25

4 4000000 0.810000 0.600 1414.73 60 10.84

6 4000000 0.810000 0.600 1414.73 60 2.14

8 4000000 0.810000 0.600 1414.73 60 0.68

10 4000000 0.810000 0.600 1414.73 60 0.28

12 75000 0.810000 0.600 1414.73 60 0.00

14 4000000 0.810000 0.600 1414.73 60 0.07

16 4000000 0.810000 0.600 1414.73 60 0.04

18 4000000 0.810000 0.600 1414.73 60 0.03

20 4000000 0.810000 0.600 1414.73 60 0.02

22 4000000 0.810000 0.600 1414.73 60 0.01

24 4000000 0.810000 0.600 1414.73 60 0.01

26 4000000 0.810000 0.600 1414.73 60 0.01

28 4000000 0.810000 0.600 1414.73 60 0.00

30 4000000 0.810000 0.600 1414.73 60 0.00

36 4000000 0.810000 0.600 1414.73 60 0.00

42 4000000 0.810000 0.600 1414.73 60 0.00

Natural Gas Flow

Pressure Drop for CPA 50E Flow Conditioners

(edit the values in Blue)







CPA 50E Pressure Loss Coefficient K = 1.6



Tube Bundle K= 0.75



Nominal Gas Compressibility Specific Line Temperature Pressure Pressure

Pipe Size Flow Factor Gravity Pressure Flowing Loss Loss

[in.] [SCFH] [Zf] [S.G.] [PSIA] [°F] [PSI] [mbar]



2 2186000 0.834691 0.600 4000 60 18.88 1301.41

3 2186000 0.834691 0.600 4000 60 3.73 257.07

4 2186000 0.834691 0.600 4000 60 1.18 81.34

6 2186000 0.834691 0.600 4000 60 0.23 16.07

8 2186000 0.834691 0.600 4000 60 0.07 5.08

10 2186000 0.834691 0.600 4000 60 0.03 2.08

12 2186000 0.834691 0.600 4000 60 0.01 1.00

14 2186000 0.834691 0.600 4000 60 0.01 0.54

16 2186000 0.834691 0.600 4000 60 0.00 0.32

18 2186000 0.834691 0.600 4000 60 0.00 0.20

20 2186000 0.834691 0.600 4000 60 0.00 0.13

22 2186000 0.834691 0.600 4000 60 0.00 0.09

24 2186000 0.834691 0.600 4000 60 0.00 0.06

26 2186000 0.834691 0.600 4000 60 0.00 0.05

28 2186000 0.834691 0.600 4000 60 0.00 0.03

30 2186000 0.834691 0.600 4000 60 0.00 0.03

36 2186000 0.834691 0.600 4000 60 0.00 0.01

42 2186000 0.834691 0.600 4000 60 0.00 0.01

GAS

Flow Rate Flow Rate Density Pipe Area Velocity

ACFH in³/sec Kg/m³ in² Ft/sec.



6719 3225 ######## 3.142 85.55

6719 3225 ######## 7.069 38.02

6719 3225 ######## 12.566 21.39

6719 3225 ######## 28.274 9.51

6719 3225 ######## 50.265 5.35

6719 3225 ######## 78.540 3.42

6719 3225 ######## 113.097 2.38

6719 3225 ######## 153.938 1.75

6719 3225 ######## 201.062 1.34

6719 3225 ######## 254.469 1.06

6719 3225 ######## 314.159 0.86

6719 3225 ######## 380.133 0.71

6719 3225 ######## 452.389 0.59

6719 3225 ######## 530.929 0.51

6719 3225 ######## 615.752 0.44

6719 3225 ######## 706.858 0.38

6719 3225 ######## 1017.876 0.26

6719 3225 ######## 1385.442 0.19

GAS

Velocity Dp Dp

m/sec pascals PSI °F °C PSIA Zf



26.076 130141.29 18.87540 60 5 4000 0.834691 0

11.589 25706.92 3.72847 0.834691 0 0.834691

6.519 8133.83 1.17971 0.840811 5 0.840811

2.897 1606.68 0.23303 0.84693 10 0.84693

1.630 508.36 0.07373 0.855022 15 0.855022

1.043 208.23 0.03020 0.863115 20 0.863115

0.724 100.42 0.01456 0.871436 25 0.871436

0.532 54.20 0.00786 0.879758 30 0.879758

0.407 31.77 0.00461 0.888641 35 0.888641

0.322 19.84 0.00288 0.897523 40 0.897523

0.261 13.01 0.00189 0.904484 45 0.904484

0.216 8.89 0.00129 0.911445 50 0.911445

0.181 6.28 0.00091

0.154 4.56 0.00066

0.133 3.39 0.00049

0.116 2.57 0.00037

0.080 1.24 0.00018

0.059 0.67 0.00010

anyless









SUMMARY OUTPUT



Regression Statistics

Multiple R 0.99774

R Square 0.995485

0.994984

Adjusted R Square

0.000366

Standard Error

Observations 11



ANOVA

df SS MS F Significance F

Regression 1 0.000266 0.000266 1984.465 7.23E-12

Residual 9 1.21E-06 1.34E-07

Total 10 0.000267



Standard Error t Stat

Coefficients Lower 95.0%pper 95.0%

P-value Lower 95%Upper 95% U

Intercept 0.965508 0.000207 4673.535 4.79E-30 0.96504 0.965975 0.96504 0.965975

X Variable 10.000311 6.98E-06 44.54733 7.23E-12 0.000295 0.000327 0.000295 0.000327

Steam Flow

Pressure Drop for CPA 50E Flow Conditioners

(edit the values in Blue)









CPA 50E Pressure Loss Coefficient K = 1.6



Tube Bundle K= 0.75

Nominal Steam Line Temperature Pressure Pressure

Pipe Size Flow Rate Pressure Flowing Loss Loss

[in.] [PPH] [PSIA] [°F] [PSI] [mbar]



2 21548 160 750 57.66 3975.54

3 21548 160 750 11.39 785.29

4 21548 160 750 3.60 248.47

6 21548 160 750 0.71 49.08

8 21548 160 750 0.23 15.53

10 21548 160 750 0.09 6.36

12 21548 160 750 0.04 3.07

14 21548 160 750 0.02 1.66

16 21548 160 750 0.01 0.97

18 21548 160 750 0.01 0.61

20 21548 160 750 0.01 0.40

22 21548 160 750 0.00 0.27

24 21548 160 750 0.00 0.19

26 21548 160 750 0.00 0.14

28 21548 160 750 0.00 0.10

30 21548 160 750 0.00 0.08

36 21548 160 750 0.00 0.04

42 21548 160 750 0.00 0.02

Note: This table is for saturated and superheated steam from 0 - 2400 PSIA

Steam

Flow Rate Flow Rate Density Density Pipe Area

PPH in³/sec lb/ft³ Kg/m³ in²



21548.0 45884.839 0.22541 3.61077 3.14

21548.0 45884.839 0.22541 3.61077 7.07

21548.0 45884.839 0.22541 3.61077 12.57

21548.0 45884.839 0.22541 3.61077 28.27

21548.0 45884.839 0.22541 3.61077 50.27

21548.0 45884.839 0.22541 3.61077 78.54

21548.0 45884.839 0.22541 3.61077 113.10

21548.0 45884.839 0.22541 3.61077 153.94

21548.0 45884.839 0.22541 3.61077 201.06

21548.0 45884.839 0.22541 3.61077 254.47

21548.0 45884.839 0.22541 3.61077 314.16

21548.0 45884.839 0.22541 3.61077 380.13

21548.0 45884.839 0.22541 3.61077 452.39

21548.0 45884.839 0.22541 3.61077 530.93

21548.0 45884.839 0.22541 3.61077 615.75

21548.0 45884.839 0.22541 3.61077 706.86

21548.0 45884.839 0.22541 3.61077 1017.88

21548.0 45884.839 0.22541 3.61077 1385.44

ASME 1967 Steam Equation: for saturated an







Steam Pressure Temperature vg r

Velocity Velocity Dp Dp Flowing Flowing

Ft/sec. m/sec pascals PSI Pa °K ft³/lbm kg/m³



1217.13 370.982 397553.75 57.66030 1103161.12 672.039 4.436301 3.61077

540.95 164.881 78529.14 11.38969 1103161.12 672.039 4.436301 3.61077

304.28 92.746 24847.11 3.60377 1103161.12 672.039 4.436301 3.61077

135.24 41.220 4908.07 0.71186 1103161.12 672.039 4.436301 3.61077

76.07 23.186 1552.94 0.22524 1103161.12 672.039 4.436301 3.61077

48.69 14.839 636.09 0.09226 1103161.12 672.039 4.436301 3.61077

33.81 10.305 306.75 0.04449 1103161.12 672.039 4.436301 3.61077

24.84 7.571 165.58 0.02402 1103161.12 672.039 4.436301 3.61077

19.02 5.797 97.06 0.01408 1103161.12 672.039 4.436301 3.61077

15.03 4.580 60.59 0.00879 1103161.12 672.039 4.436301 3.61077

12.17 3.710 39.76 0.00577 1103161.12 672.039 4.436301 3.61077

10.06 3.066 27.15 0.00394 1103161.12 672.039 4.436301 3.61077

8.45 2.576 19.17 0.00278 1103161.12 672.039 4.436301 3.61077

7.20 2.195 13.92 0.00202 1103161.12 672.039 4.436301 3.61077

6.21 1.893 10.35 0.00150 1103161.12 672.039 4.436301 3.61077

5.41 1.649 7.85 0.00114 1103161.12 672.039 4.436301 3.61077

3.76 1.145 3.79 0.00055 1103161.12 672.039 4.436301 3.61077

2.76 0.841 2.04 0.00030 1103161.12 672.039 4.436301 3.61077

m Equation: for saturated and superheated steam from 0 to 2400 psia: Flow Measurement Engineering Handbook , R.W. Miller 2nd Edition, pp 2-59 th







r Vr Pr I1 Tr x B11 B12 B21



lb/ft³



0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

0.22541 87.3657 0.049872 4.260321 1.038219 0.971248 0.066703759 1.388983801 0.083901043

W. Miller 2nd Edition, pp 2-59 thru 2-60







B22 B23 B31 B32 B41 B42 B51 B52 B53









0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

0.02614671 -0.03373439 0.45209189 0.10690366 -0.59753367 -0.08847536 0.59580516 -0.51593034 0.20750211

B61 B62 B71 B72 B81 B82 B90 B91 B92









0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

0.11906103 -0.09867174 0.16839988 -0.05809438 0.00655239 0.00057102 193.658756 -1388.52243 4126.60722

B93 B94 B95 B96 BB61 BB71 BB81 BB82 l0









-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

-6508.21168 5745.98405 -2693.08837 523.571862 0.40060739 0.08636082 -0.85323229 0.34602089 15.7437333

l1 l2 p1









-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148

-34.1706198 19.3138071 1.08547148


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