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Basic Formulas of Heat Exchanger Designs

Explore List of 49 Basic Formulas of Heat Exchanger Designs below. Find step-by-step solutions for each formula to enhance your Basic Formulas of Heat Exchanger Designs skills. Perfect for students, teachers, and all Basic Formulas of Heat Exchanger Designs enthusiasts.

fxAllowable Length of Tube given Temperature Difference and Thermal Expansion of Tubes
fxBaffle Spacing given Shell Area and Shell Diameter
fxBaffle Spacing given Tube Length and Number of Baffles
fxChannel Velocity of Fluid given Path Length and Plate Pressure Drop
fxEquivalent Diameter for Square Pitch in Heat Exchanger
fxEquivalent Diameter for Triangular Pitch in Heat Exchanger
fxFriction Factor in Plate Type Heat Exchanger
fxHeat Duty of Exchanger given Core Volume of Exchanger for Air Separation
fxHeat Duty of Exchanger given Core Volume of Exchanger for Hydrocarbon Separation
fxHeat Exchanger Volume for Air Separation Applications
fxHeat Exchanger Volume for Hydrocarbon Applications
fxLog Mean Temperature Difference in Plate Heat Exchanger Given Fluid Temperature and NTU
fxNumber of Baffles in Shell and Tube Heat Exchanger
fxNumber of Transfer Units for Plate Heat Exchanger
fxNumber of Tubes in Center Row Given Bundle Diameter and Tube Pitch
fxNumber of Tubes in Eight Pass Square Pitch given Bundle Diameter
fxNumber of Tubes in Eight Pass Triangular Pitch given Bundle Diameter
fxNumber of Tubes in Four Pass Square Pitch given Bundle Diameter
fxNumber of Tubes in Four Pass Triangular Pitch given Bundle Diameter
fxNumber of Tubes in One Pass Square Pitch given Bundle Diameter
fxNumber of Tubes in One Pass Triangular Pitch given Bundle Diameter
fxNumber of Tubes in Shell and Tube Heat Exchanger
fxNumber of Tubes in Six Pass Square Pitch given Bundle Diameter
fxNumber of Tubes in Six Pass Triangular Pitch given Bundle Diameter
fxNumber of Tubes in Two Pass Square Pitch given Bundle Diameter
fxNumber of Tubes in Two Pass Triangular Pitch given Bundle Diameter
fxOutlet Temperature of Fluid in Plate Heat Exchanger given NTU and Log Mean Temperature Difference
fxPath Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop
fxPressure Drop in Plate Type Heat Exchanger
fxPressure Drop in Plate Type Heat Exchanger given Reynolds Number
fxPressure Drop of Vapor in Condensers given Vapors on Shell Side
fxProvision for Thermal Expansion and Contraction in Heat Exchanger
fxPumping Power Required in Heat Exchanger Given Pressure Drop
fxReynolds Number for Condensate Film Inside Vertical Tubes in Condenser
fxReynolds Number for Condensate Film Outside Vertical Tubes in Heat Exchanger
fxShell Area for Heat Exchanger
fxShell Diameter Given Shell Area and Baffle Spacing and Tube Pitch
fxShell Diameter of Heat Exchanger Given Clearance and Bundle Diameter
fxShell Side Pressure Drop in Heat Exchanger
fxStack Design Pressure Draft for Furnace
fxStack Height of Furnace given Design Pressure and Flue Gas Temperature
fxTemperature Difference Achieved given Thermal Expansion and Length of Tubes in Heat Exchanger
fxTube Side Mass Flowrate Given Pumping Power and Tube Side Pressure Drop
fxTube Side Mass Flowrate of Liquid Given Number of Tubes and Fluid Velocity
fxTube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
fxTube Side Pressure Drop in Heat Exchanger for Laminar Flow
fxTube Side Pressure Drop in Heat Exchanger for Turbulent Flow
fxTube Side Velocity of Fluid Given Mass Flowrate and Number of Tubes
fxViscosity Correction Factor for Shell and Tube Heat Exchanger
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