EXCHANGER SPECIFICATION SHEET01 Plant Item no. E-100

02 Service of Unit STEAM CONDENSATE Rev. No 0 Date - 29.01.15

03 Size Type PLATE Position horizontal

04 Surface of Unit Sq.M. Surface Per Shell

05 No. Of Units Shell Arrangement Prep. By MF

06 Ref. Dwg. App. By SS

07 P E R F O R M A N C E O F O N E U N I T

08 HOT SIDE COLD SIDE

09 Fluid Circulated FLASH STEAM CONDENSATE TURBINE CONDENSATE

10 Total fluid entering

11 Vapor Kg/Hr

12 Liquid Kg/Hr 1450 2100

17 Density Kg/M3 943 990

18 Viscosity - CST Liq..

19 Therm. Cond @ oC Kcal/hr.Mo Liq.

20 Mol. Weight 18 18

21 Sp.HeatKcal/Kg/Liq.Oc 1 1

22 Temperature In |Crit. Temp. 120 45

23 Temperature Out 47 95

24 Operating Kg/cm2 (G.) 1 2

25 Number of Passes Per Shell NA NA

26 Velocity Cross: Long: In Avg

27 Pressure Drop Allow 0.2 Calc: Allowed: 0.2

28 Fouling Resistance Hr. M2 oC/Kcal

29 Heat Exchanged - Kcal/Hr. 174000 L.M.T.D.

30 Transfer Rate - Service Kcal/hr.M2 oC Calc.

31 % Excess Surface - Required Actual

32 C O N S T R U C T I O N - E A C H S H E L L33 Design Pressure Kg/cm2 G. 6 6

34 Test Pressure Kg/cm2 G.

35 Design Temperature oC 160 110

36 Tubes na No. O.D. BWG Wall mm Length mm Pitch mm

37 plate MOCSS304 I.D. na O.D. na Thickness mm

38 Shell Cover na

39 Channel I.D. mm Channel Cover

40 Tube Sheets

42 Baffle Type Tube Supports

43 Tube To Tube Sheet Joint

44 Gaskets - MOC - Compressed Asbestos Fibre45 Connections - Shell In- " Out " Drain "

47 Corrosion Allowance - Hot Side mm cold Side mm

48 Code Requirements

49 Weights - Each Shell and Bundle Kg. Bundle Only Kg. Full of Water Kg.

50 REMARKS:

E-100

Date - 29.01.15

Sq.M.

COLD SIDE

TURBINE CONDENSATE

2100

990

1

45

95

2

Out

Calc:

9.2

Pitch mm