Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop Solution

STEP 0: Pre-Calculation Summary
Formula Used
Path Length = Plate Pressure Drop*Equivalent Diameter/(8*Friction Factor*(Fluid Density*(Channel Velocity^2))/2)
Lp = ΔPp*De/(8*Jf*(ρfluid*(up^2))/2)
This formula uses 6 Variables
Variables Used
Path Length - (Measured in Meter) - Path Length refers to the distance that the fluid travels between the plates. It represents the length of the flow path within the heat exchanger channels formed by adjacent plates.
Plate Pressure Drop - (Measured in Pascal) - Plate Pressure Drop refers to the loss of fluid pressure as the fluid flows through the channels formed by the plates.
Equivalent Diameter - (Measured in Meter) - 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.
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.
Fluid Density - (Measured in Kilogram per Cubic Meter) - Fluid Density is defined as the ratio of mass of given fluid with respect to the volume that it occupies.
Channel Velocity - (Measured in Meter per Second) - Channel Velocity refers to the average velocity of the fluid flowing through the channels formed by adjacent plates.
STEP 1: Convert Input(s) to Base Unit
Plate Pressure Drop: 2070.467 Pascal --> 2070.467 Pascal No Conversion Required
Equivalent Diameter: 16.528 Millimeter --> 0.016528 Meter (Check conversion ​here)
Friction Factor: 0.004 --> No Conversion Required
Fluid Density: 995 Kilogram per Cubic Meter --> 995 Kilogram per Cubic Meter No Conversion Required
Channel Velocity: 1.845 Meter per Second --> 1.845 Meter per Second No Conversion Required
STEP 2: Evaluate Formula
Substituting Input Values in Formula
Lp = ΔPp*De/(8*Jf*(ρfluid*(up^2))/2) --> 2070.467*0.016528/(8*0.004*(995*(1.845^2))/2)
Evaluating ... ...
Lp = 0.631470130671129
STEP 3: Convert Result to Output's Unit
0.631470130671129 Meter -->631.470130671129 Millimeter (Check conversion ​here)
FINAL ANSWER
631.470130671129 631.4701 Millimeter <-- Path Length
(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
​ 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)^-0.25+2.5)*(Fluid Density/2)*(Fluid Velocity^2)
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

Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop Formula

Path Length = Plate Pressure Drop*Equivalent Diameter/(8*Friction Factor*(Fluid Density*(Channel Velocity^2))/2)
Lp = ΔPp*De/(8*Jf*(ρfluid*(up^2))/2)

What is the Significance of Plate Pressure Drop in Plate Type Heat Exchanger?

Plate pressure drop in a plate-type heat exchanger refers to the loss of fluid pressure as the fluid flows through the channels formed by the plates. It is a measure of the resistance encountered by the fluid as it moves through the narrow passages between the plates. Plate pressure drop is a critical consideration in the design and operation of plate heat exchangers. Several factors contribute to plate pressure drop, including the fluid velocity, viscosity, flow rate, and the geometric configuration of the plates (such as plate spacing and pattern). Higher fluid velocities and more complex plate arrangements tend to increase pressure drop.

How to Calculate Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop?

Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop calculator uses Path Length = Plate Pressure Drop*Equivalent Diameter/(8*Friction Factor*(Fluid Density*(Channel Velocity^2))/2) to calculate the Path Length, The Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop formula is defined as the distance that the fluid travels between the plates. It represents the length of the flow path within the heat exchanger channels formed by adjacent plates. Path Length is denoted by Lp symbol.

How to calculate Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop using this online calculator? To use this online calculator for Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop, enter Plate Pressure Drop (ΔPp), Equivalent Diameter (De), Friction Factor (Jf), Fluid Density fluid) & Channel Velocity (up) and hit the calculate button. Here is how the Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop calculation can be explained with given input values -> 631470.1 = 2070.467*0.016528/(8*0.004*(995*(1.845^2))/2).

FAQ

What is Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop?
The Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop formula is defined as the distance that the fluid travels between the plates. It represents the length of the flow path within the heat exchanger channels formed by adjacent plates and is represented as Lp = ΔPp*De/(8*Jf*(ρfluid*(up^2))/2) or Path Length = Plate Pressure Drop*Equivalent Diameter/(8*Friction Factor*(Fluid Density*(Channel Velocity^2))/2). Plate Pressure Drop refers to the loss of fluid pressure as the fluid flows through the channels formed by the plates, 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, 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, Fluid Density is defined as the ratio of mass of given fluid with respect to the volume that it occupies & Channel Velocity refers to the average velocity of the fluid flowing through the channels formed by adjacent plates.
How to calculate Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop?
The Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop formula is defined as the distance that the fluid travels between the plates. It represents the length of the flow path within the heat exchanger channels formed by adjacent plates is calculated using Path Length = Plate Pressure Drop*Equivalent Diameter/(8*Friction Factor*(Fluid Density*(Channel Velocity^2))/2). To calculate Path Length of Fluid in Plate Heat Exchanger Given Channel Velocity and Plate Pressure Drop, you need Plate Pressure Drop (ΔPp), Equivalent Diameter (De), Friction Factor (Jf), Fluid Density fluid) & Channel Velocity (up). With our tool, you need to enter the respective value for Plate Pressure Drop, Equivalent Diameter, Friction Factor, Fluid Density & Channel Velocity 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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