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Heat Exchanger Specification Sheet
Prepared By: Job No.: Company By: Ref. No.: Address: Proposal No.: Plant Address: Date: Rev. No.: Service of Units: Item No.: Surf/unit(eff.) ft2 Shells/unit Surf/shell(eff.) ft2 PERFORMANCE OF ONE UNIT Fluid allocation Shell Side Tube Side Fluid Name Fluid Quantity, Total lb/h Vapor (In/Out) lb/h Liquid lb/h Noncondensable lb/h Operating Temperature (In/Out) F Dew/Bubble point F Density (Vap/Liq) lb/ft3 Viscosity point cp Molecular wt, Vap Molecular wt, NC Specific Heat BTU/(lb*F) Thermal Conductivity BTU/(ft*h*F) Latent heat BTU/lb Pressure psi Velocity ft/s Pressure drop, allow./calc. psi Fouling resist. (min) ft2*h*F/BTU Heat exchanged BTU/h MTD corrected F Transfer rate, Service Dirty Clean BTU/(h*ft2*F) CONSTRUCTION OF ONE SHELL Sketch Shell Side Tube Side Design/Test Pressure psi Design Temperature F Number passes per shell Corrosion Allowance in Connections Inlet in Size/rating Outlet in Nominal Intermediate Tube No.: OD: Tks:in Length:in Pitch: Tube type: Material: Tube Pattern: Shell: ID: OD:in Shell Cover: Channel or Bonnet: Channel Cover: Tubesheet-stationary: Tubesheet-floating: Floating head cover: Impingement protection: Baffle-crossing: Type: Cut(%d): Spacing c/c: Baffle-long: Seal type: Inlet:in Supports-tube: U-bend: Type: Bypass seal: Tube-tubsheet joint: Expansion joint: Type: RhoV2-Inlet nozzle: Bundle entrance: Bundle exit: lb/(ft*s2) Gaskets - Shell side: Tube side: Floating head: Code requirements: TEMA class: Weight/Shell: Filled with water: Bundle: lb Remarks:
