Nothing Special   »   [go: up one dir, main page]

Line Sizing Single Phase Fluid Flow: Chemical Engineering Calculations

Download as xlsx, pdf, or txt
Download as xlsx, pdf, or txt
You are on page 1of 2

Line Sizing Single Phase Fluid Flow

CheCalc.com

Chemical Engineering Calculations


User Input Cell
Pipe Data
Pipe Inner Diameter
Pipe Roughness

52.5 mm
0.04572 mm

Fluid Data
Flowrate
Viscosity
Density

2700.0 Kg/h
0.13512 cP
567.00 Kg/m^3

Step 1 : Calculate Reynold's Number


Pipe Cross Sectional Area
Volumetric Flow
Fluid Velocity
Reynold's Number

0.0022 m^2
4.7619 m^3/h
0.61 m/s
134,615

Step 2 : Calculate Friction Factor


For Laminar Flow
Friction Factor, f

for Re < 2100


0.00048

For Turbulent Flow

For Re > 4000

Pipe Roughness/ Pipe ID

0.00087

Using Colebrook Equation


Friction factor value

0.02113

Using Churchill Equation


A
B
Friction Factor
Flow Regime
Friction factor selected

3.98.E+20
1.33E-09
0.02129
Turbulent
0.02113

Step 3 : Calculate Pressure Drop


Using Darcy-Weisbach equation
Pipe Length
Pressure Drop

3.5 m
0.00149 bar/ 100 m

Line Sizing Single Phase Fluid Flow


CheCalc.com

Chemical Engineering Calculations


User Input Cell
Pipe Data
Pipe Inner Diameter
Pipe Roughness

2.75 inch
0.0018 inch

Fluid Data
Flowrate
Viscosity
Density

5000 lb/h
1 cP
62.4 lb/ft^3

Step 1 : Calculate Reynold's Number


Pipe Cross Sectional Area
Volumetric Flow
Fluid Velocity
Reynold's Number

0.0412 ft^2
80.1282 ft^3/h
0.54 ft/sec
11,484

Step 2 : Calculate Friction Factor


For Laminar Flow
Friction Factor, f

for Re < 2100


0.00557

For Turbulent Flow

For Re > 4000

Pipe Roughness/ Pipe ID

0.00065

Using Colebrook Equation


Friction factor value

0.03084

Using Churchill Equation


A
B
Friction Factor
Flow Regime
Friction factor selected

1.94.E+19
1.69E+08
0.03105
Turbulent
0.03084

Step 3 : Calculate Pressure Drop


Using Darcy-Weisbach equation
Pipe Length
Pressure Drop

100 ft
0.02637 psi/ 100 ft

You might also like