公稱直徑

管程數

管子數量

換熱麵積 公稱值/計算值

管程通道截麵積 管程通道流速為0.5m/sec時的流量m/hr

公稱壓力

管子長度（m）

φ25×2.5

1500

2000

3000

4000

6000

φ25×2

159

1

14

1.5/1.62

2/2.17

3/3.27

0.0044/0.0049

7.92/8.82

0.25

219

1

26

3/3.00

4/4.02

6/6.06

8/8.1

0.0082/0.0090

14.76/16.20

0.6

2

26

3/3.00

4/4.02

6/6.06

8/8.81

0.0041/0.0045

7.38/8.01

1

273

1

44

5/5.08

7/5.18

10/10.26

14/13.72

21/20.63

0.013812017955/0.0152

24.84/27.36

1.6

2

40

5/4.62

6/6.19

9/9.33

12/12.47

19/18.76

0.0063/0.0069

11.24/12.42

2.5

325

1

60

7/6.93

9/9.28

14/14.00

19/18.71

28/28.13

0.0188/0.0208

33.84/37.44

0.6

2

56

6/6.47

9/8.66

13/13.05

17/17.46

36/26.26

0.0088/0.0097

15.84/17.46

1

400

1

119

14/13.47

18/18.41

28/27.76

37/37.10

55/55.8

0.0374/0.0412

67.32/74.16

1.6

2

110

13/12.70

17/17.02