Allowable Length of Tube given Temperature Difference and Thermal Expansion of Tubes
Baffle Spacing given Shell Area and Shell Diameter
Baffle Spacing given Tube Length and Number of Baffles
Channel Velocity of Fluid given Path Length and Plate Pressure Drop
Equivalent Diameter for Square Pitch in Heat Exchanger
Equivalent Diameter for Triangular Pitch in Heat Exchanger
Friction Factor in Plate Type Heat Exchanger
Heat Duty of Exchanger given Core Volume of Exchanger for Air Separation
Heat Duty of Exchanger given Core Volume of Exchanger for Hydrocarbon Separation
Heat Exchanger Volume for Air Separation Applications
Heat Exchanger Volume for Hydrocarbon Applications
Log Mean Temperature Difference in Plate Heat Exchanger Given Fluid Temperature and NTU
Number of Baffles in Shell and Tube Heat Exchanger
Number of Transfer Units for Plate Heat Exchanger
Number of Tubes in Center Row Given Bundle Diameter and Tube Pitch
Number of Tubes in Eight Pass Square Pitch given Bundle Diameter
Number of Tubes in Eight Pass Triangular Pitch given Bundle Diameter
Number of Tubes in Four Pass Square Pitch given Bundle Diameter
Number of Tubes in Four Pass Triangular Pitch given Bundle Diameter
Number of Tubes in One Pass Square Pitch given Bundle Diameter
Number of Tubes in One Pass Triangular Pitch given Bundle Diameter
Number of Tubes in Shell and Tube Heat Exchanger
Number of Tubes in Six Pass Square Pitch given Bundle Diameter
Number of Tubes in Six Pass Triangular Pitch given Bundle Diameter
Number of Tubes in Two Pass Square Pitch given Bundle Diameter
Number of Tubes in Two Pass Triangular Pitch given Bundle Diameter
Outlet Temperature of Fluid in Plate Heat Exchanger given NTU and Log Mean Temperature Difference
Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop
Pressure Drop in Plate Type Heat Exchanger
Pressure Drop in Plate Type Heat Exchanger given Reynolds Number
Pressure Drop of Vapor in Condensers given Vapors on Shell Side
Provision for Thermal Expansion and Contraction in Heat Exchanger
Pumping Power Required in Heat Exchanger Given Pressure Drop
Reynolds Number for Condensate Film Inside Vertical Tubes in Condenser
Reynolds Number for Condensate Film Outside Vertical Tubes in Heat Exchanger
Shell Area for Heat Exchanger
Shell Diameter Given Shell Area and Baffle Spacing and Tube Pitch
Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter
Shell Side Pressure Drop in Heat Exchanger
Stack Design Pressure Draft for Furnace
Stack Height of Furnace given Design Pressure and Flue Gas Temperature
Temperature Difference Achieved given Thermal Expansion and Length of Tubes in Heat Exchanger
Tube Side Mass Flowrate Given Pumping Power and Tube Side Pressure Drop
Tube Side Mass Flowrate of Liquid Given Number of Tubes and Fluid Velocity
Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
Tube Side Pressure Drop in Heat Exchanger for Laminar Flow
Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow
Tube Side Velocity of Fluid Given Mass Flowrate and Number of Tubes
Viscosity Correction Factor for Shell and Tube Heat Exchanger