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Shell Side Pressure Drop is defined as the reduction in pressure of the fluid that was allocated on the shell side of a Heat Exchanger. Check FAQs
ΔPShell=0.58Jf(LTubeLBaffle)(DsDe)(ρfluid2)(Vf2)((μfluidμWall)-0.14)
ΔPShell - Shell Side Pressure Drop?Jf - Friction Factor?LTube - Length of Tube?LBaffle - Baffle Spacing?Ds - Shell Diameter?De - Equivalent Diameter?ρfluid - Fluid Density?Vf - Fluid Velocity?μfluid - Fluid Viscosity at Bulk Temperature?μWall - Fluid Viscosity at Wall Temperature?

Pressure Drop of Vapor in Condensers given Vapors on Shell Side Example

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Here is how the Pressure Drop of Vapor in Condensers given Vapors on Shell Side equation looks like with Values.

Here is how the Pressure Drop of Vapor in Condensers given Vapors on Shell Side equation looks like with Units.

Here is how the Pressure Drop of Vapor in Condensers given Vapors on Shell Side equation looks like.

34545.0594Edit=0.580.004Edit(4500Edit200Edit)(510Edit16.528Edit)(995Edit2)(2.5Edit2)((1.005Edit1.006Edit)-0.14)
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Pressure Drop of Vapor in Condensers given Vapors on Shell Side Solution

Follow our step by step solution on how to calculate Pressure Drop of Vapor in Condensers given Vapors on Shell Side?

FIRST Step Consider the formula
ΔPShell=0.58Jf(LTubeLBaffle)(DsDe)(ρfluid2)(Vf2)((μfluidμWall)-0.14)
Next Step Substitute values of Variables
ΔPShell=0.580.004(4500mm200mm)(510mm16.528mm)(995kg/m³2)(2.5m/s2)((1.005Pa*s1.006Pa*s)-0.14)
Next Step Convert Units
ΔPShell=0.580.004(4.5m0.2m)(0.51m0.0165m)(995kg/m³2)(2.5m/s2)((1.005Pa*s1.006Pa*s)-0.14)
Next Step Prepare to Evaluate
ΔPShell=0.580.004(4.50.2)(0.510.0165)(9952)(2.52)((1.0051.006)-0.14)
Next Step Evaluate
ΔPShell=34545.0593986752Pa
LAST Step Rounding Answer
ΔPShell=34545.0594Pa

Pressure Drop of Vapor in Condensers given Vapors on Shell Side Formula Elements

Variables
Shell Side Pressure Drop
Shell Side Pressure Drop is defined as the reduction in pressure of the fluid that was allocated on the shell side of a Heat Exchanger.
Symbol: ΔPShell
Measurement: PressureUnit: Pa
Note: Value should be greater than 0.
Friction Factor
Friction Factor is a dimensionless quantity used to characterize the amount of resistance encountered by a fluid as it flows through a pipe or conduit.
Symbol: Jf
Measurement: NAUnit: Unitless
Note: Value should be greater than 0.
Length of Tube
Length of tube is the length which will be used during heat transfer in a exchanger.
Symbol: LTube
Measurement: LengthUnit: mm
Note: Value should be greater than 0.
Baffle Spacing
Baffle spacing refers to the distance between adjacent baffles within the heat exchanger. Their purpose is to create turbulence on shell side fluid.
Symbol: LBaffle
Measurement: LengthUnit: mm
Note: Value should be greater than 0.
Shell Diameter
Shell Diameter of a heat exchanger refers to the internal diameter of the cylindrical shell that houses the tube bundle.
Symbol: Ds
Measurement: LengthUnit: mm
Note: Value should be greater than 0.
Equivalent Diameter
Equivalent diameter represents a single characteristic length that takes into account the cross-sectional shape and flow path of a non-circular or irregularly shaped channel or duct.
Symbol: De
Measurement: LengthUnit: mm
Note: Value should be greater than 0.
Fluid Density
Fluid Density is defined as the ratio of mass of given fluid with respect to the volume that it occupies.
Symbol: ρfluid
Measurement: DensityUnit: kg/m³
Note: Value should be greater than 0.
Fluid Velocity
Fluid Velocity is defined as the speed with which fluid flows inside a tube or pipe.
Symbol: Vf
Measurement: SpeedUnit: m/s
Note: Value should be greater than 0.
Fluid Viscosity at Bulk Temperature
Fluid viscosity at Bulk Temperature is a fundamental property of fluids that characterizes their resistance to flow. It is defined at the bulk temperature of the fluid.
Symbol: μfluid
Measurement: Dynamic ViscosityUnit: Pa*s
Note: Value should be greater than 0.
Fluid Viscosity at Wall Temperature
Fluid Viscosity at Wall Temperature is defined at the temperature of the wall of pipe or surface at which the fluid is in contact with it.
Symbol: μWall
Measurement: Dynamic ViscosityUnit: Pa*s
Note: Value should be greater than 0.

Other Formulas to find Shell Side Pressure Drop

​Go Shell Side Pressure Drop in Heat Exchanger
ΔPShell=(8Jf(LTubeLBaffle)(DsDe))(ρfluid2)(Vf2)((μfluidμWall)-0.14)

Other formulas in Basic Formulas of Heat Exchanger Designs category

​Go Equivalent Diameter for Square Pitch in Heat Exchanger
De=(1.27DOuter)((PTube2)-0.785(DOuter2))
​Go Equivalent Diameter for Triangular Pitch in Heat Exchanger
De=(1.10DOuter)((PTube2)-0.917(DOuter2))

How to Evaluate Pressure Drop of Vapor in Condensers given Vapors on Shell Side?

Pressure Drop of Vapor in Condensers given Vapors on Shell Side evaluator uses Shell Side Pressure Drop = 0.5*8*Friction Factor*(Length of Tube/Baffle Spacing)*(Shell Diameter/Equivalent Diameter)*(Fluid Density/2)*(Fluid Velocity^2)*((Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14) to evaluate the Shell Side Pressure Drop, The Pressure Drop of Vapor in Condensers given Vapors on Shell Side formula is defined as difference between the inlet pressure and the outlet pressure of the vapor that is to be condensed in Heat exchanger called as condenser. Shell Side Pressure Drop is denoted by ΔPShell symbol.

How to evaluate Pressure Drop of Vapor in Condensers given Vapors on Shell Side using this online evaluator? To use this online evaluator for Pressure Drop of Vapor in Condensers given Vapors on Shell Side, enter Friction Factor (Jf), Length of Tube (LTube), Baffle Spacing (LBaffle), Shell Diameter (Ds), Equivalent Diameter (De), Fluid Density fluid), Fluid Velocity (Vf), Fluid Viscosity at Bulk Temperature fluid) & Fluid Viscosity at Wall Temperature Wall) and hit the calculate button.

FAQs on Pressure Drop of Vapor in Condensers given Vapors on Shell Side

What is the formula to find Pressure Drop of Vapor in Condensers given Vapors on Shell Side?
The formula of Pressure Drop of Vapor in Condensers given Vapors on Shell Side is expressed as Shell Side Pressure Drop = 0.5*8*Friction Factor*(Length of Tube/Baffle Spacing)*(Shell Diameter/Equivalent Diameter)*(Fluid Density/2)*(Fluid Velocity^2)*((Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14). Here is an example- 34545.06 = 0.5*8*0.004*(4.5/0.2)*(0.51/0.016528)*(995/2)*(2.5^2)*((1.005/1.006)^-0.14).
How to calculate Pressure Drop of Vapor in Condensers given Vapors on Shell Side?
With Friction Factor (Jf), Length of Tube (LTube), Baffle Spacing (LBaffle), Shell Diameter (Ds), Equivalent Diameter (De), Fluid Density fluid), Fluid Velocity (Vf), Fluid Viscosity at Bulk Temperature fluid) & Fluid Viscosity at Wall Temperature Wall) we can find Pressure Drop of Vapor in Condensers given Vapors on Shell Side using the formula - Shell Side Pressure Drop = 0.5*8*Friction Factor*(Length of Tube/Baffle Spacing)*(Shell Diameter/Equivalent Diameter)*(Fluid Density/2)*(Fluid Velocity^2)*((Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14).
What are the other ways to Calculate Shell Side Pressure Drop?
Here are the different ways to Calculate Shell Side Pressure Drop-
  • Shell Side Pressure Drop=(8*Friction Factor*(Length of Tube/Baffle Spacing)*(Shell Diameter/Equivalent Diameter))*(Fluid Density/2)*(Fluid Velocity^2)*((Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14)OpenImg
Can the Pressure Drop of Vapor in Condensers given Vapors on Shell Side be negative?
No, the Pressure Drop of Vapor in Condensers given Vapors on Shell Side, measured in Pressure cannot be negative.
Which unit is used to measure Pressure Drop of Vapor in Condensers given Vapors on Shell Side?
Pressure Drop of Vapor in Condensers given Vapors on Shell Side is usually measured using the Pascal[Pa] for Pressure. Kilopascal[Pa], Bar[Pa], Pound Per Square Inch[Pa] are the few other units in which Pressure Drop of Vapor in Condensers given Vapors on Shell Side can be measured.
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