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Heat Exchanger Design, Inc.
P.O.Box 524 Indianapolis, IN., 46206 Customer Plant Location Service f Unit S i of U it Size Connected in Surface/Unit(Eff) Ft2 Heat Exchanger Specification Sheet ThermalSpec No. ENAP Conoepoion, Chile Naphta Cooler N ht C l 22 x 288 Type B F S 1 Series Shell & 1 Parallel Shell Surface/Shell(Eff) 1390 Shells/Unit 1 PERFORMANCE OF ONE UNIT Fluid Allocation Shell SideTube Side Fluid Name L.S.R. Naphta Cooling Water In / Out IN OUT IN Total Flow lb/hr lb/hr Liquid Liquid Density lb/ft3 Liquid Viscosity cP Btu/lb-F Liquid Specific Heat Liquid Thermal ConductivityBtu/hr-ft-F Btu/lb Latent Heat lb/hr Vapor lb/ft3 Vapor Density p y Vapor Viscosity cP Btu/lb-F Vapor Specific Heat Vapor Thermal Conductivity Btu/hr-ft-F Vapor Mol. Weight Temperature F OperatingPressure psi(Abs) Velocity ft/sec / / Pressure Drop(Allow/Calc) Psi Fouling R i t hr-ft2-F/Btu F li Resistance h ft2 F/Bt BTU/HR MTD Heath Exchanged Transfer Rate, Service Bth/hr-ft2-F Clean CONSTRUCTIONOF ONE Shell Side Tube Side Design/Test Pressure psig 210 / Code 50 / Code Design Temperature F 220 150 No. Passes per Shell 2 6 Corrosion Allowance in 0.125 0 125 0.125 0 125 (CS) Connections Size &In (in) 3 4 Rating Out (in) 3 4 Rating 150 # RF 150 # FF Tube No. 300 OD. (in) 3/4 Thickness (in) 0.065 Pitch (in) 15/16", Tri Tube Type PLAIN Material SB111-Admilarty N/A Shell OD (in) 22" MaterialSA-53B Thickness (in) 3/8 Schedule Std Channel or Bonnet SA516-70 Channel Cover N/A Tubesheet, Stationary NRB Tubesheet, Floating NRB Impingement Protection Yes Shell Cover 45 Spacing c-c (in) 13Baffles-Cross A-36 %Cut 0 Fin/Tube 0 Fin Thickness Fin Material N/A Fin Height Tube Supports Steel Tube-Tubesheet Joint ROLLED N/A Type N/A Expansion Joint Rho-V2 Inlet Nozzle Bundle Entrance Bundle ExitGasket, Shell side DJNA Tube side DJNA Floating Head DJNA C d R i Code Requirement t ASME Section 8 Division 1 S ti 8, Di i i TEMA Class Cl R Weight / Shell (lb) 9,800 Bundle 3,800 Stress Relieve,...
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