+ All Categories
Home > Documents > Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1...

Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1...

Date post: 04-Nov-2020
Category:
Upload: others
View: 1 times
Download: 0 times
Share this document with a friend
11
1 2 3 4 5 6 610 / mm Type BEM 1 1 7 m2 1 8 9 10 11 12 13 14 15 16 C 17 C 18 / / / / 19 / / / / 20 21 22 / / / / 23 / / / / 24 25 26 27 28 Ao based 29 C 30 31 32 33 bar / / / / 34 C 35 36 mm 37 In mm 1 / / 38 1 / / 39 Nominal / / 40 OD mm Length mm mm 41 42 ID OD mm 43 SS 316L 44 SS 316L 45 - 46 Single segmen H mm 47 mm 48 49 50 51 52 - Tube Side Flat Metal Jacket Fibe 53 - 54 Not TEMA, Code only 55 kg 56 57 58 Shell Side 0 66,7 0 Pressurised Water Tube Side 985,01 973,47 0,3554 Bundle F1 8,5 986 8,5 0,0002 Remarks Filled with water Code requirements CODAP -1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 922 1787 Bundle entrance - - RhoV2-Inlet nozzle m/s - - Number passes per shell Corrosion allowance 15 500,7 0 Dirty Tube Side -1 Shell Side 1 1,5 Out 350 Transfer rate, Service Velocity Heat Exchanger Specification Sheet From: Thomas LABBE (Cell: +33.6.78.17.11.76) M. LABBE - Rue de l'Industrie - 77220 Tournan - France Our Reference: TL130030 Size Thermal conductivity Vapor (In/Out) Liquid Noncondensable W/(m*K) cp 0 61,2 Viscosity Molecular wt, Vap Dew / Bubble point PERFORMANCE OF ONE UNIT Fluid allocation Fluid name 80 kg/s bar Latent heat 160 148,5 Temperature (In/Out) Molecular wt, NC Specific heat Density (Vap / Liq) Pressure (abs) Your Reference: E22-2 Reactor Primary Heat Exchanger - F1 Case Date: 31/01/2013 Connected in Surf/shell (eff.) Shells/unit Surf/unit(eff.) m2 125,6 parallel 125,6 Ver 7000 Fluid quantity, Total 66,7 183,2 0 kg/s kg/s series 0,4661 4185,5 J/(kg*K) 66,7 986 4187,67 kg/m3 183,2 0 0 183,2 Intermediate - 25 Tks- 300 224 250 5258,1 Pressure drop, allow./calc. Fouling resist. (min) Heat exchanged Design/vac/test pressure:g 500,9 Clean CONSTRUCTION OF ONE SHELL m2*K/W bar Size/rating Sketch kW 1 83,6 W/(m2*K) Tubesheet-stationary Floating head cover Plain 232 31,25 Shell cover 610 40,5 Cut(%d) Tube type Channel or bonnet Shell Tube No. SS 316L Type SS 316L 570 480 Spacing: c/c 7000 - - - Channel cover - None Impingement protection SS 316L Material 30 25 Type Pitch Avg Tube-tubesheet joint Bypass seal Type Gaskets - Shell side Floating head Baffle-crossing - Expansion joint Baffle-long Supports-tube Exp. SS 316L kg/(m*s2) Bundle exit 911 Inlet 806,98 MTD corrected 1 0 - 250 200 0,31501 28,68499 - 712,5 29 1,28 Tubesheet-floating Tube pattern 14,81656 0,15 0,15 2500 0,6627 0,00039 0,00033 2 2500 2,31 0,38344 15,2
Transcript
Page 1: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance

1

2

3

4

5

6 610 / mm Type BEM 1 1

7 m2 1

8

9

10

11

12

13

14

15

16 C

17 C

18 / / / /

19 / / / /

20

21

22 / / / /

23 / / / /

24

25

26

27

28 Ao based

29 C

30

31

32

33 bar / / / /

34 C

35

36 mm

37 In mm 1 / /

38 1 / /

39 Nominal / /

40 OD mm Length mm mm

41

42 ID OD mm

43 SS 316L

44 SS 316L

45 -

46 Single segmental H mm

47 mm

48

49

50

51

52 - Tube Side Flat Metal Jacket Fibe

53 -

54 Not TEMA, Code only

55 kg

56

57

58

Shell Side

0

66,7

0

Pressurised Water

Tube Side

985,01 973,47

0,3554

Bundle

F1

8,5

986

8,5

0,0002

Remarks

Filled with water

Code requirements CODAP

-1

0,6445

kJ/kg

U-bend

Seal type

2

1

Connections

Design temperature

TEMA class

Weight/Shell -

kg/s

9221787 Bundle entrance

- -

RhoV2-Inlet nozzle

m/s

- -

Number passes per shell

Corrosion allowance

15

500,7

0

Dirty

Tube Side

-1

Shell Side

1

1,5

Out 350

Transfer rate, Service

Velocity

Heat Exchanger Specification Sheet

From: Thomas LABBE (Cell: +33.6.78.17.11.76)

M. LABBE - Rue de l'Industrie - 77220 Tournan - France

Our Reference: TL130030

Size

Thermal conductivity

Vapor (In/Out)

Liquid

Noncondensable

W/(m*K)

cp

0

61,2

Viscosity

Molecular wt, Vap

Dew / Bubble point

PERFORMANCE OF ONE UNIT

Fluid allocation

Fluid name

80

kg/s

bar

Latent heat

160 148,5Temperature (In/Out)

Molecular wt, NC

Specific heat

Density (Vap / Liq)

Pressure (abs)

Your Reference: E22-2 Reactor Primary Heat Exchanger - F1 Case

Date: 31/01/2013

Connected in

Surf/shell (eff.)Shells/unitSurf/unit(eff.) m2125,6

parallel

125,6

Ver7000

Fluid quantity, Total 66,7 183,2

0kg/s

kg/s

series

0,4661

4185,5J/(kg*K)

66,7

986

4187,67

kg/m3

183,2

0 0

183,2

Intermediate -

25

Tks-

300

224 250

5258,1

Pressure drop, allow./calc.

Fouling resist. (min)

Heat exchanged

Design/vac/test pressure:g

500,9 Clean

CONSTRUCTION OF ONE SHELL

m2*K/W

bar

Size/rating

Sketch

kW

1

83,6

W/(m2*K)

Tubesheet-stationary

Floating head cover

Plain

232 31,25

Shell cover610

40,5Cut(%d)

Tube type

Channel or bonnet

Shell

Tube No.

SS 316L Type

SS 316L 570

480Spacing: c/c

7000

-

-

-

Channel cover -

NoneImpingement protection

SS 316LMaterial 30

25

Type

PitchAvg

Tube-tubesheet jointBypass seal

Type

Gaskets - Shell side

Floating head

Baffle-crossing

-

Expansion joint

Baffle-long

Supports-tube

Exp.

SS 316L

kg/(m*s2)Bundle exit911

Inlet 806,98

MTD corrected

1

0

-

250

200

0,31501

28,68499

-

712,5

29

1,28

Tubesheet-floating

Tube pattern

14,81656

0,15 0,15

2500

0,6627

0,000390,00033

2

2500

2,31

0,38344

15,2

T1

S1

S2

T2

Page 2: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 3: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 4: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 5: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 6: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 7: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 8: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 9: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 10: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance
Page 11: Heat Exchanger Specification Sheet · Code requirements CODAP-1 0,6445 kJ/kg U-bend Seal type 2 1 Connections Design temperature TEMA class Weight/Shell - kg/s 1787 Bundle entrance

Recommended