background image

2  |  

Baker Hughes

© 2020 Baker Hughes Company. All rights reserved.

Table 1 - Equilibrium Moisture Contents of Natural Gases Above the Critical Temperature

PSIA

°F

14.7

100

200

300

400

500

600

700

800

900

1000

-40

9.10

1.50

0.88

0.66

0.55

0.49

0.44

0.41

0.39

0.37

0.36

-36

11.5

1.90

1.10

0.80

0.68

0.59

0.54

0.50

0.47

0.45

0.43

-32

14.4

2.40

1.30

0.99

0.82

0.72

0.65

0.60

0.57

0.54

0.51

-28

17.8

2.90

1.60

1.20

1.00

0.87

0.79

0.72

0.68

0.64

0.61

-24

22.0

3.60

2.00

1.50

1.20

1.10

0.95

0.87

0.81

0.77

0.73

-20

27.0

4.40

2.40

1.80

1.50

1.30

1.10

1.00

0.97

0.92

0.87

-16

33.1

5.40

3.00

2.20

1.80

1.50

1.40

1.20

1.20

1.10

1.00

-12

40.5

6.50

3.60

2.60

2.10

1.80

1.60

1.50

1.40

1.30

1.20

-8

49.3

7.90

4.30

3.10

2.50

2.20

1.90

1.80

1.60

1.50

1.50

-4

59.8

9.50

5.20

3.70

3.00

2.60

2.30

2.10

1.90

1.80

1.70

0

72.1

11.4

6.20

4.50

3.60

3.10

2.70

2.50

2.30

2.10

2.00

4

86.8

13.7

7.40

5.30

4.30

3.60

3.20

2.90

2.70

2.50

2.40

8

104

16.4

8.80

6.30

5.10

4.30

3.80

3.40

3.20

3.00

2.80

12

124

19.5

10.5

7.50

6.00

5.10

4.50

4.00

3.70

3.50

3.30

16

148

23.2

12.4

8.80

7.00

5.90

5.20

4.70

4.30

4.00

3.80

20

176

27.4

14.6

10.4

8.20

7.00

6.10

5.50

5.10

4.70

4.40

24

208

32.4

17.2

12.2

9.70

8.20

7.20

6.40

5.90

5.50

5.10

28

246

38.1

20.2

14.3

11.3

9.50

8.30

7.50

6.80

6.30

5.90

32

289

44.7

23.7

16.7

13.2

11.1

9.70

8.70

7.90

7.30

6.90

34

313

48.4

25.6

18.0

14.2

11.9

10.4

9.30

8.50

7.90

7.40

36

339

52.4

27.7

19.4

15.3

12.9

11.2

10.0

9.20

8.50

7.90

38

367

56.6

29.9

20.1

16.5

13.9

12.1

10.8

9.80

9.10

8.50

40

396

61.1

32.2

22.6

17.8

14.9

13.0

11.6

10.6

9.80

9.10

The Table above can be used as follows:

Assume that the pipeline pressure is 1000 psig at 40°F. This gas can hold 9.1 Ib./mmscf of water.
Assume that the pressure will be cut from 1000 psig to 100 psig at the supply regulator.
Assume that for every 100 psjg drop in pressure the gas will drop 7°F in temperature. In this case, the temperature will 

drop from 40°F to -23°F (1000 psig - 100 psig / 100 psig x 7°F =63°F).
From the table, look up 100 psig and -23°F (or the closest value). If the number is below 7 lb./mmscf, water will fallout of 

the gas and the desiccant should be replaced once a year to prevent problems as a result of freezing.

The above test procedure indicates the predicted service life of the Becker FD-1500 filter/dryer cartridge assembly. 

 

Should you require any additional information or assistance please feel free to contact Becker Technical assistance.

Reference: Gas Engineers Handbook 1st Edition

Reviews: