Calculation of Power Required in Fan, Blower, and Compressor

The function of Fans, Blowers, and Compressors is to increase the mechanical energy of gases.

Fans, Blowers, and Compressors are used for different services based on the required discharge pressure of the gases.

If the Required Discharge Pressure is less than 3.45 kPa g, then a Fan is used.

A Blower is used when the Required Discharge Pressure is higher than 3.45 kPa g. The maximum discharge pressure of the blower is 1 atm g.

Furthermore, if the Required Discharge Pressure exceeds 2 atm (absolute), then a Compressor is used. The discharge pressure of the compressor ranges from 2 atm a to thousands of atmospheres.

Calculation of Power Required by Fan

Fans are mainly classified into two categories

  1. Centrifugal fans and
  2. Axial flow fans.

The efficiency of a fan ranges from 40 to 70%, depending on its specific speed.

The following equation determines the power input to a fan

Equation determining the power input to a fan

Where,
P0= Power required by fan, kW
qv = Capacity of fan, m3/h
pd = Discharge pressure of fan, cm WC (gauge pressure)
= Sum of pressure and velocity head, developed by the fan, cm WC
η = Efficiency of fan

Calculation of Power Required in Blower and in Adiabatic Compressor

Blowers are always operated in an adiabatic manner.

Many compressors, such as air compressors up to 10 bar g, are also operated in an adiabatic manner. In an adiabatic compressor, jacketed cooling is not provided. While in other types; polytropic and isothermal compressors, jacketed cooling is provided around the compressor section.

In an isothermal compressor, the inlet temperature of a gas is equal to the outlet temperature of a gas. If both temperatures are not the same even after providing jacket cooling, the compressor is called a polytropic compressor.

PVT Relationship for Adiabatic Compression

Equations representing the Pressure-Volume-Temperature (PVT) relationship for adiabatic compression

Where,
k = Cp/Cv= ratio of specific heat at constant pressure to specific heat at constant volume
p2, p1 = outlet/inlet pressure of gas, kPa
V2, V1 = outlet/inlet volume of gas, m3/kmol
T2, T1 = outlet/inlet temperatures of gas, K

Blower Power Calculation (kw)

Power required in single-stage blowers or single-stage adiabatic compressors (Blower Power Calculation Formula)

Power required in single-stage blowers or single-stage adiabatic compressors (Blower Power Calculation Formula)

Where,
P0 = Power required, kW
p1, p2 = Absolute inlet pressure, kPa
qv1 = Volumetric flow rate of gas based on inlet condition, m3/h
η = Efficiency of blower

Discharge temperature of gas from the blower or single-stage adiabatic compressor

Equation for the discharge temperature of gas from a blower or single-stage adiabatic compressor

The value of k ranges from 1.39 to 1.41 for air and perfect diatomic gases.

X factor calculation for the value of k=1.395

Equation for calculating the X factor with a specific heat ratio 
𝑘
=
1.395
k=1.395, showing the relationship between pressure ratio and the heat capacity ratio in determining the performance or efficiency of a thermodynamic process.

Where,
k = 1.395 for air or a diatomic gas
r = Compression ratio

Power required for the blower and adiabatic compressor

Equation for calculating the power required for a blower or adiabatic compressor, incorporating variables such as pressure ratio, volumetric flow rate, efficiency, and the heat capacity ratio, typically expressed to determine the energy consumption in compressing a gas.

Other gases have a value of k in the range of 1 to 1.4.

Power required by the blower or adiabatic compressor, for the gases having a value of k other than k =1.395, is given by the following equation:

Power required by the blower or adiabatic compressor, for the gases having a value of k other than k =1.395

Where, d = 2.292 [(k – 1)/k]

Values of XG/X and d can be obtained from the graph XG/X vs k and d vs k available in the book (Perry, R. H., and Green D, Perry’s Chemical Engineer’s Handbook, 6th Ed., McGraw-Hill Education, USA, 1984.) for the different values of k and different values of r.

Multistage Compressor

For a multistage compressor with N stages of compression in which
1. Adiabatic compression takes place in each stage,
2. Near equal work done in each stage (i.e., equal compression ratio in each stage; r) and
3. Intercooling is provided between every two stages of compression to the same inlet
gas temperature (T1),

We can calculate the power requirement using the following equation:

For the multistage compressor, we can calculate the discharge temperature from the last stage using the following equation.

Equation for calculating the discharge temperature from the last stage of a multistage compressor, taking into account the temperature rise in each stage, pressure ratio, and the heat capacity ratio

Where, N = Number of Stages

For the multistage compressor, the following equation can predict the discharge temperature from the last stage.

Formula for predicting the discharge temperature from the last stage of a multistage compressor, based on the pressure ratios and temperature rise across all stages

Summary

Calculations for determining the power required in fans, blowers, and compressors. It covers key concepts like pressure, flow rate, and efficiency. Detailed formulas and practical examples guide engineers in process design and equipment selection. This article helps optimize energy use. It enhances system performance in chemical engineering applications. This is applicable whether dealing with low-pressure fans or high-pressure compressors.

References

Sinnott, R. K., Coulson & Richardson’s Chemical Engineering, Vol. 6, Asian Book Private Ltd., Revised 2nd Ed., New Delhi, 1998.

Perry, R. H., and Green D, Perry’s Chemical Engineer’s Handbook, 6th Ed.,
McGraw-Hill Education, USA, 1984.

Thakore, S. B. and B. B. I. (2015). Introduction to process engineering and design. McGraw-Hill Education.

Read Also:

Bernoulli’s Equation Derivation and Application

Difference Between Centrifugal Pump and Reciprocating Pump

Helmholtz Free Energy and Gibbs Free Energy

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