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 In recent times, compressed air systems
(CAS) are being rightfully criticized for poor
energy efficiency.
 It is actually the compressed air application
that is defining the energy efficiency of the
CAS, which also means that any further
effort related to the energy savings must be
focused on the application (end-use) side.
 The study reveals inefficient usage, leak
problems and also poor system control and
monitoring, which is clearly not consistent
with established best practice
 The exergy represents the amount of useful
energy, which can be theoretically converted
to mechanical energy.
 In order to emphasize the inefficiency of the
typical end-use a simplified system analysis
based on work ability (exergy) of the
compressed air was carried out.
 It can be easily shown that in case of CAS
only the pressure dependent term is crucial.
 The equation above shows the mathematical
formulation of exergy based on ideal gas approach.
 This approach is suitable for further investigation of
the work ability change of compressed air over each
of the key elements of the compressed air system
characterized by relevant efficiency.
 Key components of Compressed Air Systems
are as follows:
 Compressor
 Dryer
 Pressure regulator
 The efficiency of conversion of the input electric
power to the output compressed air power can
be described by Equation
 The long term averaged values of the existing oil
free centrifugal compressor installed in the
company :
Pout = 6.75 bar(a),
Va = 0.45 Nm3/s,
Eel = 220 kW.
 Thus, the efficiency of the process is 0.39.
 The efficiency of the dryer is expressed by
Equation
 The outlet exergy of CA can be modified by the
dryer pressure drop only or a combination of
purge air loss and the pressure drop depending
on the dryer type.
 Purge air loss in Company A is approximately 5%
of the inlet mass rate and a pressure drop of 2%
of the inlet pressure.
 Under these conditions, dryer efficiency is 0.94.
 Important element of the CAS is the pressure
regulator which stabilize the pressure level
before final application by reducing pressure
of the incoming compressed air
 The efficiency of the process can be also
described by Equation given below depending
on the pressure regulator type.
 Pressure regulator has an efficiency of 0.95.
 Two important compressed air applications
i.e. pneumatic actuation and pure
cooling/drying, are discussed from the point
of the view of the usage of the useful energy.
 Pneumatic actuation, which is supposed to
be a relatively efficient CA application, will
be detailed for the example of the double
acting rodless cylinder.
 The efficiency of the process can be defined by
Equation
 Here the numerator represents useful work W
done by pneumatic forces F and denominator
means total energy of incoming compressed air
to the working chamber, which can be utilized
for the useful work from the start of the motion
at time t1 till the end of motion at time t2.
 The efficiency in this case is 0.1-0.2.
 Dryers and pressure regulators have
efficiencies in an acceptable range
 The efficiency of compressor though not very
good is considerable
 Efficiency of applications of compressed air
is very poor
 Although the efficiency of the actuation can
vary depending on the situation under
investigation, any results will make the total
efficiency of the CAS (product of particular
efficiencies) tend towards zero.
 As a considerable part of electric energy is
transferred into pressure energy of the
medium and this high pressure energy is not
utilized at the application side, compressed
air usage leads to the most of the energy
being wasted.
 The application of the exergy analysis has
shown that the critical point of the
compressed air system is the application
side, which is a limiting factor of the
efficiency of the whole compressed air
system.
 Future optimization of the compressed air
system should be focused on the application
side, where a high potential of energy savings is
projected.
 In order to quantify air consumption of the CAS,
different types of pneumatic actuators are
modeled and the overall air consumption is
compared to the real data available.
 The process includes collection of available
information such as pressure level of the
particular end application, geometric
parameters, working time/cycling, shift patterns
etc. which is necessary for a mathematical
model.
 There is a multi-purpose usage of compressed air
in the company
 The breakdown of air usage is:
 fluidizing (conveying/cleaning – at two different
pressure levels) - 67.12%
 open blow applications (e.g. bowl feeding, index
sensor blow-off) - 12.76%
 filter pulsing - 5.92%
 actuation - 3.82%
 controllers sealing - 3.5%
 hoisting - 3.46%
 air whip cleaning - 1.77%
 PLC sealing 1.53%
 air gun 0.12%.
 Based on the available information company has applied
leak elimination technique and pressure decay
measurement
 The difference between the model and measured values
was initially almost 30%.
 However, based on the leak estimation technique
described below, the difference has been reduced to
6.7%, as summarized in Table below
 The company also implements a pressure
decay measurement, which can be related to
the leakage effect.
 At end of a production period, all machines
are stopped and the system is pressurized up
to a pressure of 6.6 bar.
 The estimate of leak flow rate is directly
proportional to Volume, and so has a
sensitivity of 1, thus, there is a potential for
improvement of the technique by detailed
volume estimation.
 Based on the model, almost 80% of the
fluidizing air is used at pressure slightly
higher than atmospheric and this air has
been generated with considerably higher
pressure level than actually required, thus a
more detailed study of the process and
possible local blower implementation could
result in a substantial energy saving
opportunity.
 The compressed air systems are complex and any
simplified approach will naturally lead to the
differences between reality and the model.
 However, it has been shown that it is possible to
understand system behavior based on a suitable
mathematical tool.
 The investigation revealed poor compressed air
energy utilization on the application side
resulting in low overall system efficiency and
several energy savings opportunities are
suggested for specific applications found in the
investigated companies.
Energy conservation in compressed air systems

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Energy conservation in compressed air systems

  • 1.
  • 2.  In recent times, compressed air systems (CAS) are being rightfully criticized for poor energy efficiency.  It is actually the compressed air application that is defining the energy efficiency of the CAS, which also means that any further effort related to the energy savings must be focused on the application (end-use) side.  The study reveals inefficient usage, leak problems and also poor system control and monitoring, which is clearly not consistent with established best practice
  • 3.
  • 4.  The exergy represents the amount of useful energy, which can be theoretically converted to mechanical energy.  In order to emphasize the inefficiency of the typical end-use a simplified system analysis based on work ability (exergy) of the compressed air was carried out.  It can be easily shown that in case of CAS only the pressure dependent term is crucial.
  • 5.  The equation above shows the mathematical formulation of exergy based on ideal gas approach.  This approach is suitable for further investigation of the work ability change of compressed air over each of the key elements of the compressed air system characterized by relevant efficiency.
  • 6.  Key components of Compressed Air Systems are as follows:  Compressor  Dryer  Pressure regulator
  • 7.  The efficiency of conversion of the input electric power to the output compressed air power can be described by Equation  The long term averaged values of the existing oil free centrifugal compressor installed in the company : Pout = 6.75 bar(a), Va = 0.45 Nm3/s, Eel = 220 kW.  Thus, the efficiency of the process is 0.39.
  • 8.  The efficiency of the dryer is expressed by Equation  The outlet exergy of CA can be modified by the dryer pressure drop only or a combination of purge air loss and the pressure drop depending on the dryer type.  Purge air loss in Company A is approximately 5% of the inlet mass rate and a pressure drop of 2% of the inlet pressure.  Under these conditions, dryer efficiency is 0.94.
  • 9.  Important element of the CAS is the pressure regulator which stabilize the pressure level before final application by reducing pressure of the incoming compressed air  The efficiency of the process can be also described by Equation given below depending on the pressure regulator type.  Pressure regulator has an efficiency of 0.95.
  • 10.  Two important compressed air applications i.e. pneumatic actuation and pure cooling/drying, are discussed from the point of the view of the usage of the useful energy.  Pneumatic actuation, which is supposed to be a relatively efficient CA application, will be detailed for the example of the double acting rodless cylinder.
  • 11.  The efficiency of the process can be defined by Equation  Here the numerator represents useful work W done by pneumatic forces F and denominator means total energy of incoming compressed air to the working chamber, which can be utilized for the useful work from the start of the motion at time t1 till the end of motion at time t2.  The efficiency in this case is 0.1-0.2.
  • 12.  Dryers and pressure regulators have efficiencies in an acceptable range  The efficiency of compressor though not very good is considerable  Efficiency of applications of compressed air is very poor  Although the efficiency of the actuation can vary depending on the situation under investigation, any results will make the total efficiency of the CAS (product of particular efficiencies) tend towards zero.
  • 13.  As a considerable part of electric energy is transferred into pressure energy of the medium and this high pressure energy is not utilized at the application side, compressed air usage leads to the most of the energy being wasted.  The application of the exergy analysis has shown that the critical point of the compressed air system is the application side, which is a limiting factor of the efficiency of the whole compressed air system.
  • 14.
  • 15.  Future optimization of the compressed air system should be focused on the application side, where a high potential of energy savings is projected.  In order to quantify air consumption of the CAS, different types of pneumatic actuators are modeled and the overall air consumption is compared to the real data available.  The process includes collection of available information such as pressure level of the particular end application, geometric parameters, working time/cycling, shift patterns etc. which is necessary for a mathematical model.
  • 16.  There is a multi-purpose usage of compressed air in the company  The breakdown of air usage is:  fluidizing (conveying/cleaning – at two different pressure levels) - 67.12%  open blow applications (e.g. bowl feeding, index sensor blow-off) - 12.76%  filter pulsing - 5.92%  actuation - 3.82%  controllers sealing - 3.5%  hoisting - 3.46%  air whip cleaning - 1.77%  PLC sealing 1.53%  air gun 0.12%.
  • 17.  Based on the available information company has applied leak elimination technique and pressure decay measurement  The difference between the model and measured values was initially almost 30%.  However, based on the leak estimation technique described below, the difference has been reduced to 6.7%, as summarized in Table below
  • 18.  The company also implements a pressure decay measurement, which can be related to the leakage effect.  At end of a production period, all machines are stopped and the system is pressurized up to a pressure of 6.6 bar.  The estimate of leak flow rate is directly proportional to Volume, and so has a sensitivity of 1, thus, there is a potential for improvement of the technique by detailed volume estimation.
  • 19.  Based on the model, almost 80% of the fluidizing air is used at pressure slightly higher than atmospheric and this air has been generated with considerably higher pressure level than actually required, thus a more detailed study of the process and possible local blower implementation could result in a substantial energy saving opportunity.
  • 20.  The compressed air systems are complex and any simplified approach will naturally lead to the differences between reality and the model.  However, it has been shown that it is possible to understand system behavior based on a suitable mathematical tool.  The investigation revealed poor compressed air energy utilization on the application side resulting in low overall system efficiency and several energy savings opportunities are suggested for specific applications found in the investigated companies.

Notes de l'éditeur

  1. The problem lies in the design of the CAS as plant design has implicitly assumed that compressed air is free at point of use and cheap to produce centrally, and so energy saving aspects are rarely considered at the process planning stage.
  2. The installed dryer is a heated desiccant type, so inclusion of power consumption of the heating elements into dryer efficiency calculation is possible, but unlike the compressor, electrical energy does not directly change the exergy.
  3. Please note that possible low efficiency of the regulation does not mean a poor quality regulator, but work ability destruction according to the need of the relevant application.
  4. It is obvious that this kind of data is not always easy to obtain resulting in an imprecise model, but a better understanding of the process is still possible as shown in the results below.