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Tube Side Pressure Drop is the difference between inlet and outlet pressure of the tube side fluid in a shell and tube heat exchanger. Check FAQs
ΔPTube Side=NTube Pass(8Jf(LTubeDinner)(μfluidμWall)-0.14+2.5)(ρfluid2)(Vf2)
ΔPTube Side - Tube Side Pressure Drop?NTube Pass - Number of Tube-Side Passes?Jf - Friction Factor?LTube - Length of Tube?Dinner - Pipe Inner Diameter?μfluid - Fluid Viscosity at Bulk Temperature?μWall - Fluid Viscosity at Wall Temperature?ρfluid - Fluid Density?Vf - Fluid Velocity?

Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow Example

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With units
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Here is how the Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow equation looks like with Values.

Here is how the Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow equation looks like with Units.

Here is how the Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow equation looks like.

186854.5662Edit=4Edit(80.004Edit(4500Edit11.5Edit)(1.005Edit1.006Edit)-0.14+2.5)(995Edit2)(2.5Edit2)
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Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow Solution

Follow our step by step solution on how to calculate Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow?

FIRST Step Consider the formula
ΔPTube Side=NTube Pass(8Jf(LTubeDinner)(μfluidμWall)-0.14+2.5)(ρfluid2)(Vf2)
Next Step Substitute values of Variables
ΔPTube Side=4(80.004(4500mm11.5mm)(1.005Pa*s1.006Pa*s)-0.14+2.5)(995kg/m³2)(2.5m/s2)
Next Step Convert Units
ΔPTube Side=4(80.004(4.5m0.0115m)(1.005Pa*s1.006Pa*s)-0.14+2.5)(995kg/m³2)(2.5m/s2)
Next Step Prepare to Evaluate
ΔPTube Side=4(80.004(4.50.0115)(1.0051.006)-0.14+2.5)(9952)(2.52)
Next Step Evaluate
ΔPTube Side=186854.56616131Pa
LAST Step Rounding Answer
ΔPTube Side=186854.5662Pa

Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow Formula Elements

Variables
Tube Side Pressure Drop
Tube Side Pressure Drop is the difference between inlet and outlet pressure of the tube side fluid in a shell and tube heat exchanger.
Symbol: ΔPTube Side
Measurement: PressureUnit: Pa
Note: Value should be greater than 0.
Number of Tube-Side Passes
Number of Tube-Side Passes refers to the number of divisions in which the tubes are divided in the heat exchanger.
Symbol: NTube Pass
Measurement: NAUnit: Unitless
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.
Pipe Inner Diameter
Pipe inner diameter is the inner diameter where in the flow of fluid takes place. Pipe thickness is not taken into account.
Symbol: Dinner
Measurement: LengthUnit: mm
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.
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.

Other Formulas to find Tube Side Pressure Drop

​Go Tube Side Pressure Drop in Heat Exchanger for Laminar Flow
ΔPTube Side=NTube Pass(8Jf(LTubeDinner)(μfluidμWall)-0.25+2.5)(ρfluid2)(Vf2)
​Go Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid
ΔPTube Side=PpρfluidMflow

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 Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow?

Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow evaluator uses Tube Side Pressure Drop = Number of Tube-Side Passes*(8*Friction Factor*(Length of Tube/Pipe Inner Diameter)*(Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14+2.5)*(Fluid Density/2)*(Fluid Velocity^2) to evaluate the Tube Side Pressure Drop, The Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow formula is defined as Difference between inlet pressure and the outlet pressure of the fluid that is allocated on tube side of shell and tube heat exchanger. For Turbulent flow the viscosity Correction Exponent becomes (-0.14). Tube Side Pressure Drop is denoted by ΔPTube Side symbol.

How to evaluate Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow using this online evaluator? To use this online evaluator for Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow, enter Number of Tube-Side Passes (NTube Pass), Friction Factor (Jf), Length of Tube (LTube), Pipe Inner Diameter (Dinner), Fluid Viscosity at Bulk Temperature fluid), Fluid Viscosity at Wall Temperature Wall), Fluid Density fluid) & Fluid Velocity (Vf) and hit the calculate button.

FAQs on Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow

What is the formula to find Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow?
The formula of Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow is expressed as Tube Side Pressure Drop = Number of Tube-Side Passes*(8*Friction Factor*(Length of Tube/Pipe Inner Diameter)*(Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14+2.5)*(Fluid Density/2)*(Fluid Velocity^2). Here is an example- 186854.6 = 4*(8*0.004*(4.5/0.0115)*(1.005/1.006)^-0.14+2.5)*(995/2)*(2.5^2).
How to calculate Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow?
With Number of Tube-Side Passes (NTube Pass), Friction Factor (Jf), Length of Tube (LTube), Pipe Inner Diameter (Dinner), Fluid Viscosity at Bulk Temperature fluid), Fluid Viscosity at Wall Temperature Wall), Fluid Density fluid) & Fluid Velocity (Vf) we can find Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow using the formula - Tube Side Pressure Drop = Number of Tube-Side Passes*(8*Friction Factor*(Length of Tube/Pipe Inner Diameter)*(Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.14+2.5)*(Fluid Density/2)*(Fluid Velocity^2).
What are the other ways to Calculate Tube Side Pressure Drop?
Here are the different ways to Calculate Tube Side Pressure Drop-
  • Tube Side Pressure Drop=Number of Tube-Side Passes*(8*Friction Factor*(Length of Tube/Pipe Inner Diameter)*(Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^-0.25+2.5)*(Fluid Density/2)*(Fluid Velocity^2)OpenImg
  • Tube Side Pressure Drop=(Pumping Power*Fluid Density)/Mass FlowrateOpenImg
Can the Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow be negative?
No, the Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow, measured in Pressure cannot be negative.
Which unit is used to measure Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow?
Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow 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 Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow can be measured.
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