Shell And Tube He Spec Sheet Master

HEAT EXCHANGER SPECIFICATION SHEET 1 2 3 4

Custome rAddress

5 6 7

Service of Unit Siz e Surf/Unit(Gross/Eff)

8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30

Job No. Reference No. Proposal No. Date

Plant Location Type

(Hor/Vert) Sq. Ft; Shells/Unit PERFORMANCE OF UNIT Shell Side

Fluid Allocation Fluid Name Fluid Quantity, Total lb/hr Vapor (In/Out) Liquid Steam Water Noncondensable

Rev . Item No. Connected Parallel In Surf Shell Gross/Eff)

Series Sq. Ft.

Tube Side

Temperature (In/Out),°F Specific Gravity Viscosity, Liquid, Cp Molecular Weight, Vapor Molecular Weight, Noncondensable Specific Heat, Btu/Lb °F Thermal Conductivity, Btu Ft/Hr Sq Ft °F Latent Heat, Btu/lb@ °F Inlet Pressure, psig Velocity, Ft/S Pressure Drop, Allow./Calc., psig Fouling Resistance (Min.) Heat Exchanged Transfer Rate, Service

Btu/Hr. MTD (Corrected) Clean

31 32 33 34 35 36 37 38 39

CONSTRUCTION OF ONE SHELL Shell Side Design/Test Pressure Psig Design Temperature °F Passes per Shell No. Corrosion Allowance In. Connections In Size & Out Rating Intermediate

40 41 42 43 44 45 46 47 48 49 50 51 52

Tube OD In.; BWG No. Type (Min/Avg) Tube Bare / Finned Thk Shell ID OD In . Channel of Bonnett Tubesheet-Stationary Floating Head Cover BafflesType Cross BafflesLong Bypass Seal Arrangement Expansion Joint Gaskets-Shell Side Tube Side Code Requirements ASME Sect. Weight/Shell Filled with Water

53 54

Remarks

Tube Side

°F Btu/Hr Sq Ft °F Sketch (Bundle/Nozzle Orientation)

FFt;Pitch I 30°  60°  90°  45°  n Material Shell Cover (Integ.) (Remov.) Channel Cover Tubesheet-Floating Impingement Protection % Cut Diam/Area) Spacing: Inle In. c/c t Seal Type Tube - Tubesheet Joint Roll Type Flanged and Flued / Flanged Only / Bellows Floating Head TEMA Class Bundle Lb.