Viscosity Correction Factor for Shell and Tube Heat Exchanger Calculator

✖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.ⓘ Fluid Viscosity at Bulk Temperature [μ_fluid]			+10% -10%
✖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.ⓘ Fluid Viscosity at Wall Temperature [μ_Wall]			+10% -10%

✖Viscosity Correction Factor is ratio of fluid viscosity at mean temperature to fluid viscosity at the wall temperature.ⓘ Viscosity Correction Factor for Shell and Tube Heat Exchanger [μ_Correction]

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Viscosity Correction Factor for Shell and Tube Heat Exchanger

Formula

`"μ"_{"Correction"} = ("μ"_{"fluid"}/"μ"_{"Wall"})^0.14`

Example

`"0.999861"=("1.005Pa*s"/"1.006Pa*s")^0.14`

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Viscosity Correction Factor for Shell and Tube Heat Exchanger Solution

STEP 0: Pre-Calculation Summary

Formula Used

Viscosity Correction Factor = (Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^0.14
μ_Correction = (μ_fluid/μ_Wall)^0.14
This formula uses 3 Variables

Variables Used

Viscosity Correction Factor - Viscosity Correction Factor is ratio of fluid viscosity at mean temperature to fluid viscosity at the wall temperature.
Fluid Viscosity at Bulk Temperature - (Measured in Pascal Second) - 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.
Fluid Viscosity at Wall Temperature - (Measured in Pascal Second) - 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.

STEP 1: Convert Input(s) to Base Unit

Fluid Viscosity at Bulk Temperature: 1.005 Pascal Second --> 1.005 Pascal Second No Conversion Required
Fluid Viscosity at Wall Temperature: 1.006 Pascal Second --> 1.006 Pascal Second No Conversion Required

STEP 2: Evaluate Formula

Substituting Input Values in Formula

μ_Correction = (μ_fluid/μ_Wall)^0.14 --> (1.005/1.006)^0.14

Evaluating ... ...

μ_Correction = 0.999860775469323

STEP 3: Convert Result to Output's Unit

0.999860775469323 --> No Conversion Required

FINAL ANSWER

0.999860775469323 ≈ 0.999861 <-- Viscosity Correction Factor

(Calculation completed in 00.004 seconds)

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< 25 Basic Formulas Of Heat Exchanger Designs Calculators

Pressure Drop of Vapor in Condensers given Vapors on Shell Side

Go 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)

Shell Side Pressure Drop in Heat Exchanger

Go 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)

Tube Side Pressure Drop in Heat Exchanger for Turbulent Flow

Go 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)

Tube Side Pressure Drop in Heat Exchanger for Laminar Flow

Reynolds Number for Condensate Film Outside Vertical Tubes in Heat Exchanger

Go Reynold Number = 4*Mass Flowrate/(pi*Pipe Outer Diameter*Number of Tubes*Fluid Viscosity at Bulk Temperature)

Reynolds Number for Condensate Film Inside Vertical Tubes in Condenser

Go Reynold Number = 4*Mass Flowrate/(pi*Pipe Inner Diameter*Number of Tubes*Fluid Viscosity at Bulk Temperature)

Number of Tubes in Shell and Tube Heat Exchanger

Go Number of Tubes = 4*Mass Flowrate/(Fluid Density*Fluid Velocity*pi*(Pipe Inner Diameter)^2)

Shell Area for Heat Exchanger

Go Shell Area = (Tube Pitch-Pipe Outer Diameter)*Shell Diameter*(Baffle Spacing/Tube Pitch)

Stack Design Pressure Draft for Furnace

Go Draft Pressure = 0.0342*(Stack Height)*Atmospheric Pressure*(1/Ambient Temperature-1/Flue Gas Temperature)

Number of Transfer Units for Plate Heat Exchanger

Go Number of Transfer Units = (Outlet Temperature-Inlet Temperature)/Log Mean Temperature Difference

Equivalent Diameter for Triangular Pitch in Heat Exchanger

Go Equivalent Diameter = (1.10/Pipe Outer Diameter)*((Tube Pitch^2)-0.917*(Pipe Outer Diameter^2))

Equivalent Diameter for Square Pitch in Heat Exchanger

Go Equivalent Diameter = (1.27/Pipe Outer Diameter)*((Tube Pitch^2)-0.785*(Pipe Outer Diameter^2))

Viscosity Correction Factor for Shell and Tube Heat Exchanger

Go Viscosity Correction Factor = (Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^0.14

Pumping Power Required in Heat Exchanger Given Pressure Drop

Go Pumping Power = (Mass Flowrate*Tube Side Pressure Drop)/Fluid Density

Heat Exchanger Volume for Hydrocarbon Applications

Go Heat Exchanger Volume = (Heat Duty of Heat Exchanger/Log Mean Temperature Difference)/100000

Heat Exchanger Volume for Air Separation Applications

Go Heat Exchanger Volume = (Heat Duty of Heat Exchanger/Log Mean Temperature Difference)/50000

Provision for Thermal Expansion and Contraction in Heat Exchanger

Go Thermal Expansion = (97.1*10^-6)*Length of Tube*Temperature Difference

Number of Tubes in Eight Pass Triangular Pitch given Bundle Diameter

Go Number of Tubes = 0.0365*(Bundle Diameter/Pipe Outer Diameter)^2.675

Number of Tubes in Six Pass Triangular Pitch given Bundle Diameter

Go Number of Tubes = 0.0743*(Bundle Diameter/Pipe Outer Diameter)^2.499

Number of Tubes in Four Pass Triangular Pitch given Bundle Diameter

Go Number of Tubes = 0.175*(Bundle Diameter/Pipe Outer Diameter)^2.285

Number of Tubes in One Pass Triangular Pitch given Bundle Diameter

Go Number of Tubes = 0.319*(Bundle Diameter/Pipe Outer Diameter)^2.142

Number of Tubes in Two Pass Triangular Pitch given Bundle Diameter

Go Number of Tubes = 0.249*(Bundle Diameter/Pipe Outer Diameter)^2.207

Number of Tubes in Center Row Given Bundle Diameter and Tube Pitch

Go Number of Tubes in Vertical Tube Row = Bundle Diameter/Tube Pitch

Number of Baffles in Shell and Tube Heat Exchanger

Go Number of Baffles = (Length of Tube/Baffle Spacing)-1

Shell Diameter of Heat Exchanger Given Clearance and Bundle Diameter

Go Shell Diameter = Shell Clearance+Bundle Diameter

Viscosity Correction Factor for Shell and Tube Heat Exchanger Formula

Viscosity Correction Factor = (Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^0.14
μ_Correction = (μ_fluid/μ_Wall)^0.14

What is Viscosity of fluid?

Viscosity is a measure of a fluid's resistance to flow. It determines how easily a fluid can be deformed or how smoothly it can move within itself. In simple terms, it is the internal friction within a fluid that opposes its motion.

Factors that influence viscosity include temperature, pressure, and the presence of dissolved solids or gases in the fluid. As temperature increases, the viscosity of most fluids tends to decrease.

What is the significance of Viscosity Correction Factor?

Viscosity correction factors are used to account for the changes in fluid viscosity due to variations in temperature. The viscosity of fluids typically decreases as temperature increases. When calculating the performance of a heat exchanger, it's important to consider the impact of changing viscosity on heat transfer and pressure drop. The viscosity correction factor is a mathematical adjustment used to incorporate the effects of varying viscosity into heat exchanger calculations.

How to Calculate Viscosity Correction Factor for Shell and Tube Heat Exchanger?

Viscosity Correction Factor for Shell and Tube Heat Exchanger calculator uses Viscosity Correction Factor = (Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^0.14 to calculate the Viscosity Correction Factor, The Viscosity Correction Factor For Shell and Tube Heat Exchanger formula is defined as the ratio of viscosity of fluid at bulk temperature by viscosity of fluid at the wall temperature in pipe flow. Viscosity being function of temperature, the correction factor becomes important parameter. Viscosity Correction Factor is denoted by μ_Correction symbol.

How to calculate Viscosity Correction Factor for Shell and Tube Heat Exchanger using this online calculator? To use this online calculator for Viscosity Correction Factor for Shell and Tube Heat Exchanger, enter Fluid Viscosity at Bulk Temperature (μ_fluid) & Fluid Viscosity at Wall Temperature (μ_Wall) and hit the calculate button. Here is how the Viscosity Correction Factor for Shell and Tube Heat Exchanger calculation can be explained with given input values -> 0.999861 = (1.005/1.006)^0.14.

FAQ

What is Viscosity Correction Factor for Shell and Tube Heat Exchanger?

The Viscosity Correction Factor For Shell and Tube Heat Exchanger formula is defined as the ratio of viscosity of fluid at bulk temperature by viscosity of fluid at the wall temperature in pipe flow. Viscosity being function of temperature, the correction factor becomes important parameter and is represented as μ_Correction = (μ_fluid/μ_Wall)^0.14 or Viscosity Correction Factor = (Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^0.14. 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 & 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.

How to calculate Viscosity Correction Factor for Shell and Tube Heat Exchanger?

The Viscosity Correction Factor For Shell and Tube Heat Exchanger formula is defined as the ratio of viscosity of fluid at bulk temperature by viscosity of fluid at the wall temperature in pipe flow. Viscosity being function of temperature, the correction factor becomes important parameter is calculated using Viscosity Correction Factor = (Fluid Viscosity at Bulk Temperature/Fluid Viscosity at Wall Temperature)^0.14. To calculate Viscosity Correction Factor for Shell and Tube Heat Exchanger, you need Fluid Viscosity at Bulk Temperature (μ_fluid) & Fluid Viscosity at Wall Temperature (μ_Wall). With our tool, you need to enter the respective value for Fluid Viscosity at Bulk Temperature & Fluid Viscosity at Wall Temperature and hit the calculate button. You can also select the units (if any) for Input(s) and the Output as well.

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