Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid Calculator

✖Pumping Power in a heat exchanger refers to the energy required to circulate the heat transfer fluid (typically a liquid) through the exchanger.ⓘ Pumping Power [P_p]			+10% -10%
✖Fluid Density is defined as the ratio of mass of given fluid with respect to the volume that it occupies.ⓘ Fluid Density [ρ_fluid]			+10% -10%
✖Mass Flowrate is the mass of a substance that passes per unit of time.ⓘ Mass Flowrate [M_flow]			+10% -10%

✖Tube Side Pressure Drop is the difference between inlet and outlet pressure of the tube side fluid in a shell and tube heat exchanger.ⓘ Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid [ΔP_{Tube Side}]

⎘ Copy

👎

Formula

✖

Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid

Formula

`"ΔP"_{"Tube Side"} = ("P"_{"p"}*"ρ"_{"fluid"})/"M"_{"flow"}`

Example

`"186854.6Pa"=("2629.11W"*"995kg/m³")/"14kg/s"`

Calculator

LaTeX

Reset

👍

Download Heat Exchangers Formula PDF PDF Image

Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid Solution

STEP 0: Pre-Calculation Summary

Formula Used

Tube Side Pressure Drop = (Pumping Power*Fluid Density)/Mass Flowrate
ΔP_{Tube Side} = (P_p*ρ_fluid)/M_flow
This formula uses 4 Variables

Variables Used

Tube Side Pressure Drop - (Measured in Pascal) - Tube Side Pressure Drop is the difference between inlet and outlet pressure of the tube side fluid in a shell and tube heat exchanger.
Pumping Power - (Measured in Watt) - Pumping Power in a heat exchanger refers to the energy required to circulate the heat transfer fluid (typically a liquid) through the exchanger.
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.
Mass Flowrate - (Measured in Kilogram per Second) - Mass Flowrate is the mass of a substance that passes per unit of time.

STEP 1: Convert Input(s) to Base Unit

Pumping Power: 2629.11 Watt --> 2629.11 Watt No Conversion Required
Fluid Density: 995 Kilogram per Cubic Meter --> 995 Kilogram per Cubic Meter No Conversion Required
Mass Flowrate: 14 Kilogram per Second --> 14 Kilogram per Second No Conversion Required

STEP 2: Evaluate Formula

Substituting Input Values in Formula

ΔP_{Tube Side} = (P_p*ρ_fluid)/M_flow --> (2629.11*995)/14

Evaluating ... ...

ΔP_{Tube Side} = 186854.603571429

STEP 3: Convert Result to Output's Unit

186854.603571429 Pascal --> No Conversion Required

FINAL ANSWER

186854.603571429 ≈ 186854.6 Pascal <-- Tube Side Pressure Drop

(Calculation completed in 00.004 seconds)

You are here -

Home » Engineering » Chemical Engineering » Process Equipment Design » Heat Exchangers » Basic Formulas Of Heat Exchanger Designs » Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid

Credits

Created by Rishi Vadodaria

Malviya National Institute Of Technology (MNIT JAIPUR ), JAIPUR

Rishi Vadodaria has created this Calculator and 200+ more calculators!

Verified by Vaibhav Mishra

DJ Sanghvi College of Engineering (DJSCE), Mumbai

Vaibhav Mishra has verified this Calculator and 200+ more calculators!

< 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

Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid Formula

Tube Side Pressure Drop = (Pumping Power*Fluid Density)/Mass Flowrate
ΔP_{Tube Side} = (P_p*ρ_fluid)/M_flow

What is Pumping Power?

Pumping power in a heat exchanger is the energy required to move the heat transfer fluid through the system. It represents the work done by a pump to circulate the fluid, overcoming resistance and maintaining the desired flow rate. Pumping power is typically measured in watts or horsepower and is influenced by factors such as flow rate and pressure differential across the heat exchanger. Minimizing pumping power is essential for optimizing the energy efficiency of the heat exchange process.

What is the Significance of Tube Side Pressure Drop?

The tube side pressure drop in a heat exchanger is a critical parameter that holds significant implications for the design, operation, and efficiency of the heat exchange process.
Tube side pressure drop directly affects the energy efficiency of the heat exchanger. Higher pressure drops require more energy to maintain fluid flow through the system, leading to increased pump power consumption.
Excessive pressure drop can result in higher operating costs due to increased energy consumption. Minimizing pressure drop is crucial for optimizing the cost-effectiveness of the heat exchanger operation.

How to Calculate Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid?

Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid calculator uses Tube Side Pressure Drop = (Pumping Power*Fluid Density)/Mass Flowrate to calculate the Tube Side Pressure Drop, The Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid formula is defined as the decrease in pressure that occurs as a fluid flows through the tubes of the heat exchanger. Tube Side Pressure Drop is denoted by ΔP_{Tube Side} symbol.

How to calculate Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid using this online calculator? To use this online calculator for Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid, enter Pumping Power (P_p), Fluid Density (ρ_fluid) & Mass Flowrate (M_flow) and hit the calculate button. Here is how the Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid calculation can be explained with given input values -> 186854.6 = (2629.11*995)/14.

FAQ

What is Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid?

The Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid formula is defined as the decrease in pressure that occurs as a fluid flows through the tubes of the heat exchanger and is represented as ΔP_{Tube Side} = (P_p*ρ_fluid)/M_flow or Tube Side Pressure Drop = (Pumping Power*Fluid Density)/Mass Flowrate. Pumping Power in a heat exchanger refers to the energy required to circulate the heat transfer fluid (typically a liquid) through the exchanger, Fluid Density is defined as the ratio of mass of given fluid with respect to the volume that it occupies & Mass Flowrate is the mass of a substance that passes per unit of time.

How to calculate Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid?

The Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid formula is defined as the decrease in pressure that occurs as a fluid flows through the tubes of the heat exchanger is calculated using Tube Side Pressure Drop = (Pumping Power*Fluid Density)/Mass Flowrate. To calculate Tube Side Pressure Drop given Pumping Power and Mass Flowrate of Fluid, you need Pumping Power (P_p), Fluid Density (ρ_fluid) & Mass Flowrate (M_flow). With our tool, you need to enter the respective value for Pumping Power, Fluid Density & Mass Flowrate and hit the calculate button. You can also select the units (if any) for Input(s) and the Output as well.

How many ways are there to calculate Tube Side Pressure Drop?

In this formula, Tube Side Pressure Drop uses Pumping Power, Fluid Density & Mass Flowrate. We can use 2 other way(s) to calculate the same, which is/are as follows -

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)
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)

Home

FREE PDFs

🔍 Search