Pneumatic and hydraulic maintenance questions.
MODULE TITLE : APPLICATIONS OF PNEUMATICS AND
HYDRAULICS
TOPIC TITLE : SPECIFICATION, SELECTION AND
MAINTENANCE OF EQUIPMENT
LESSON 1 : COMPRESSOR SELECTION
APH - 3 - 1
© Teesside University 2011
Published by Teesside University Open Learning (Engineering)
School of Science & Engineering
Teesside University
Tees Valley, UK
TS1 3BA
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INTRODUCTION ________________________________________________________________________________________
In this lesson we are going to consider the principles of compressor selection.
Generally, more than one type of compressor will meet a practical requirement
and the choice will be made after consideration of some or all of the factors
outlined in the following text.
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YOUR AIMS ________________________________________________________________________________________
On completion of this lesson you should be able to:
• appreciate the importance of correct compressor selection
• understand the different kinds of duty to which a compressor may be
subjected
• correctly select a compressor to meet the volume and pressure
requirements of a given system
• interpret a duty cycle chart
• explain the operation of typical compressor cooling systems.
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CHOICE OF COMPRESSOR ________________________________________________________________________________________
The choice of a compressor for any installation may be either a relatively
simple or an extremely complex task, depending upon the size and complexity
of the plant being supplied. It is safe to say that the choice of a compressor for
any installation is best undertaken with the aid of expert advice from
compressor manufacturers. Reputable suppliers are only too willing to assist,
as it is in their own interest to do so. However, at the end of the day, the
responsibility for correct selection lies with the selecting engineer: therefore
knowledge of the key factors to be considered is essential.
If the compressor being selected is for the purpose of supplying air-power to a
complete plant, its importance must be fully understood. Should the
compressor fail because it is not suited to the particular situation, the whole
plant may be brought to a standstill. It can be seen that care and attention to
detail, during the selection of such a vital piece of equipment, is essential.
From previous work, we have seen that there are several different types of
compressor and many different designs. The different designs have often been
developed as a response to changing needs with respect to quality, quantity and
pressure requirements of systems.
It is important to be able to analyse the needs of the compressed air user, to
ensure the correct matching of machine type to the kind of work that it is to
undertake. Therefore we could define one of the prime criteria of compressor
selection as the purpose of the compressor.
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DURATION OF THE LOAD
There are different kinds of duty for compressors. At one end of the scale is
the small garage compressor, used to inflate car tyres, which is only used for
short periods throughout the day. At the other end of the scale is the process
compressor in a chemical plant, which is supplying high quantities of air
24 hours a day, 7 days a week. These are extremes of use, but they highlight
the fact that a compressor's duty cycle is extremely varied and has an important
bearing on selection.
It is possible to break down duty types into four categories which are outlined
below.
Occasional Intermittent Use
This is the kind of machine found, for example, in small garages and training
workshops – typically the kind of application where usage is only in the order
of 10 to 15 minutes per hour during an 8-hour day.
Traditionally, small single-stage single-acting reciprocating compressors,
which are air-cooled and are supplied as packaged units, with drive motor,
receiver and all controls mounted, are used for this application.
The major drawback with this kind of machine tends to be the noise level.
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Normal Industrial Use
Most industrial compressors come into this category. Normally they operate
continuously throughout an 8-hour shift, and experience periods of both light
and heavy-duty running, depending upon the demand for air.
This obviously calls for a machine which is built for a much longer life than
occasional duty; but its total number of running hours per week is still
relatively small.
Machines which are suitable for this category are:
• multistage
• reciprocating
• vane and screw compressors, the final choice being dependent upon other
factors.
Day and Night Shift Working
This duty is yet again more arduous; but the types of machine selected are
often the same, the main difference being the way the machines are operated
and maintained. It could be that two machines are installed, the usage being
alternated, one for day shift and one for night shift.
Continuous Process Work
This is the most difficult duty of all. It often means supplying air 24 hours per
day for 7 days per week and often every week of the year, apart from an annual
shut-down period of two or three weeks.
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This kind of duty will almost certainly entail selection of a machine which is
of a heavy-duty type and extremely reliable in operation. In most cases several
machines are used and the usage varied, by this means a 'back up' machine is
provided.
Outline two benefits of using two compressors on an alternating basis for this
continuous duty.
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Two benefits of using two compressors on an alternating basis for such continuous duty are:
• A back-up compressor is always available should one machine fail.
• Maintenance may be carried out on the machine that is not in use.
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PRESSURE CAPABILITY
If a compressor is supplying air for power, its pressure capability is of prime
importance.
The machine must be capable of generating air at a greater pressure than the
user requires, to cater for pressure drops within the system.
It must also be capable of operating at this pressure as efficiently as possible.
What is the effect on the flow-rate of a single-stage reciprocating compressor operating
at a higher pressure than its design limit?
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There will be a reduction in its flow-rate due to the re-expansion of the clearance space
gases causing a reduction in volumetric efficiency.
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There are advantages to be gained by selecting a compressor from a
manufacturer's standard pressure range. Typically for power air (7 to 9 bar),
these would be:
• cheaper price
• quicker delivery
• wider choice of models.
It will be found that a machine such as this will normally satisfy most plant
requirements.
If there is a special requirement for higher pressures to service one or two
pieces of equipment, local high-pressure booster compressors may be used to
draw a small supply of air from the main air-line, and increase its pressure to
satisfy this need.
CAPACITY
Selecting the correct capacity of machine to satisfy demand is not as easy as it
may seem. To estimate the amount of compressed air that a plant will use
poses several problems.
There are three main difficulties to overcome:
• estimating the consumption of each piece of equipment
• analysing the duty cycle of each piece of equipment
• estimating the amount of leakage within the system.
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Let us look at each of the above difficulties in greater detail.
• Machine manufacturer's catalogues often give details of air consumption.
This may be in terms of FAD or compressed air, but it is unlikely that this
data will be available for every piece of equipment. Therefore, some
calculation based on machine observations will be necessary.
• It is unlikely that each piece of equipment will be in operation at the same
time, so their periods of use will have to be analysed.
• The rate of leakage within the system will have to be calculated. Most
compressed air systems have leakage which is typically between 5% and
15% of total consumption and in older systems may be appreciably more.
DUTY CYCLE CHART
When analysing the duty cycle, it will be useful to produce a chart giving a
visual representation of demand for air throughout the day. This is done by
plotting demand for air on the vertical axis and time on the horizontal, as
shown in FIGURE 1.
FIG. 1 Typical Demand for Air Throughout an 8 Hour Day
Air flow
m3 min–1
B re
a k B re
a k
L u n ch
Start 1 2 3 4 5 6 7 8 End Time of day - hours
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EXPANSION
When considering a compressor installation it is wise to obtain information
with regard to future expansion of the plant. It may be possible to cater for this
future need, as it will certainly have a bearing on the compressor selection.
There have been many cases where, 12 months after a system has been
installed, it is unable to satisfy demand because additional equipment has been
added.
It's also important that air consumption be expressed in terms of FAD as the
following example illustrates.
Example
A machine is rated at using compressed air at the rate of 1 m3 min–1 at 7 bar
gauge. Convert this to FAD.
Solution
Because FAD is air at atmospheric pressure we can calculate its value using
the gas laws. Assuming no appreciable temperature change,
Working in absolute values:
V p V
p2 1 1
2
7 1 01 1
1 01
7 93
= = +( ) ×
=
.
.
. m min FAD3 –1
p V p V1 1 2 2=
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It is obvious from this calculation that care must be taken to convert any
machine consumption figures in compressed air to FAD.
NUMBER OF COMPRESSORS REQUIRED
It may be found that after estimating the demand for air, it may be met by a
single compressor. While on the face of it this may be a simple solution, it
may not be the best option. There are various reasons why this is so but one
consideration is that, when the distribution system covers a large area and long
pipe runs are encountered, excessive pressure drops can occur. This problem
can be reduced by using two compressors sited at opposite ends of the
distribution system.
TYPES OF COMPRESSOR REQUIRED
We previously dealt with compressor types. A short review of their suitability
for a specific purpose may be advantageous at this point.
The choice of a compressor type to supply normal production shop air at
approximately 7 bar gauge is dependent upon various factors.
Reciprocating Piston Machines
These machines have managed to service this area reliably for many years.
Their operation and maintenance requirements are fairly well understood by
most maintenance engineers.
They are readily available from many manufacturers and spares are often in
good supply.
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Choice of control and output flow is comparatively straightforward. Smaller
models can be air cooled, while most medium to larger sizes are water cooled.
The main disadvantages are that they:
• provide pulsating air
• are noisy in operation
• require heavier foundations than other types
• produce air which is often oil loaded.
However, some of these disadvantages can often be overcome by correct siting
and installation.
Vane Compressors
These are normally chosen for smaller plants, although some larger capacity
models are available.
They are quieter in operation than reciprocating compressors and don't have
special foundation requirements.
These machines are normally supplied as packaged units that only require
bolting down and the services connecting up.
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Screw Compressors
These machines are the main competitor to the reciprocating compressor for
producing air-power to medium-sized plants. Their increasing popularity is
associated with the following advantages:
• the air is pulsation free
• they are relatively quiet in operation
• no special foundations are required.
While the routine maintenance requirements of this type of machine are fairly
simple, a major overhaul is complex and is normally a task for the
manufacturer or specialist service company.
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COMPRESSOR COOLING ________________________________________________________________________________________
Cooling for compressors is an important consideration. It is essential that a
compressor is run at its optimum temperature, if efficiency in operation and
long life are to be obtained. The type of cooling may be either water or air.
AIR COOLING
This is the simplest and least expensive method, both in terms of initial cost
and also maintenance.
There are two types of air-cooling system:
• Natural cooling: the compressor jacket is finned, so heat is dissipated
directly to the surroundings by a combination of conduction and
convection. This method is limited to small low-duty compressors. The
degree of cooling obtained is dependent upon ambient temperatures.
Therefore, accurate control of temperature is not possible.
• Forced-draught cooling: again the jacket is finned, but the cooling air is
blown across the fins by a fan, giving a greater cooling effect. This
method is more effective than the first since a degree of control can be
achieved by controlling the speed of the fan or the angle of the fan blades.
This method can be used for small and some medium sizes of machine.
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WATER COOLING
Water cooling is used for most medium and larger machines. It tends to
provide lower cooling temperatures which do not fluctuate as much as those
for air-cooled types.
It is possible to re-cycle the heat removed in the cooling water and use it to do
useful work. This is obviously more energy efficient.
The three most commonly used methods of water cooling are:
• mains water
• thermo-siphon
• forced circulation.
Each system will be considered separately.
Mains Water
In this system water is drawn from the main, passed through the compressor
cooling jacket picking up heat, and finally ejected directly to waste. A flow
control valve, which has its opening controlled by a temperature sensor within
the compressor water jacket, regulates the rate of flow to maintain a constant
temperature. FIGURE 2 illustrates the principle.
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FIG. 2 Mains Water Cooling
List two possible disadvantages of this system.
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• High volumes of water are passed through the machine: this can be expensive.
• If the water is untreated, it may cause scaling and fouling of the compressor cooling
jacket and pipework, reducing efficiency. Freezing in winter may also be a problem.
Water supply
Waste
Temperature sensor
Bypass for manual control
Flow indicator
Strainer Self acting temperature
control valve
Compressor
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Thermo-siphon
This system is a semi-closed loop system as shown in FIGURE 3, in which the
cooling water is kept in a holding tank at some elevated position. Evaporative
losses are topped up via a mains-water ball-float valve, which is similar to that
used in a toilet flush water system. Cool water from the bottom of the tank
flows into the cooling jacket inlet, where it picks up heat, rises due to
convection, and finally flows back to the tank via the top jacket outlet: hence a
continuous circulation is maintained. The heat is dissipated from the surface
of the water and also through the tank sides.
A temperature sensor is normally incorporated within the tank. Should the
temperature exceed a pre-determined maximum, it would open a valve,
allowing mains water to flow into the tank. This would displace the hot water
in the tank, forcing it through an overflow, hence cooling the system.
FIG. 3 Thermo-siphon Cooling System
Mains
Ball valve
Overflow
Cool in
Warm out
Temperature sensor
Compressor
Water tank
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List two advantages of this system compared to the mains-water system.
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• Less water is used, making it cheaper to operate.
• The water may be treated to prevent scaling and freezing.
Forced Circulation
FIGURE 4 shows a forced circulation cooling system. This is a closed-loop
system, which is the most practical method of cooling larger compressors.
Water is pumped through the compressor, picking up heat, and then passed to a
three way valve, where, depending upon its temperature, it is either sent to the
cooler or diverted back to the pump inlet.
On start-up the compressor will be cold. To allow it to reach its normal
operating temperature as quickly as possible, the cooling water is only
circulated around the compressor jacket, and does not receive any cooling.
When the normal operating temperature is reached a sensor opens the three-
way valve and diverts the flow to the cooler. Heat is removed here and the
water is re-circulated back to the pump inlet.
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FIG. 4 Forced Circulation Cooling System
This system is normally used for larger machines with intercoolers and
aftercoolers.
With all water-cooled systems, it is important that the flow of water is
monitored, and with the mains and forced cooling systems, it is essential that
water is flowing before the machine is started up. This is often ensured by
interlocking a flow switch with the compressor starter controls.
Pump
To cooler
From cooler
Warm out
Compressor
Cool in
3-way valve
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FINANCIAL CONSIDERATIONS ________________________________________________________________________________________
In most industrial plants an air compressor is an essential piece of equipment.
Therefore, the capital outlay for a good reliable machine is easily justified.
Unfortunately this is only part of the cost.
Other costs to be considered are:
• the compressor building
• installation costs
• running costs
• maintenance
• spares
• depreciation of capital.
OTHER CONSIDERATIONS
Other factors which should be taken into consideration when selecting a
compressor are:
• the space available – this should include ease of access for maintenance
purposes
• the choice of a permanent or temporary installation
• the type of prime-mover to be used – these may be electric motor, internal
combustion engine or turbine
• compatability with other compressors already on site.
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SELF-ASSESSMENT QUESTIONS ________________________________________________________________________________________
1. Explain briefly why a compressor must be capable of producing air at a
higher pressure than the end-user requires.
2. List three reasons why it may be difficult to obtain an accurate value for
the demand for compressed air.
3. Explain briefly the purpose of a three-way valve in a forced-cooling
system.
4. List two advantages of utilising compressors, of the same type and
design, for a factory air supply.
5. Explain the main advantage water cooling has over air cooling.
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ANSWERS TO SELF-ASSESSMENT QUESTIONS ________________________________________________________________________________________
1. A compressor must be capable of producing air at a higher pressure than
the end-user requires, to cater for pressure losses within the system.
2. The three main reasons for difficulties with accurate calculations of flow
demand are:
• it can be difficult to obtain information on the flow requirement for
every piece of equipment
• it is unlikely that each piece of equipment will be operated at the
same time
• the leakage rate of the system must be taken into account.
3. The purpose of the three-way valve is to give a choice of flow-path for the
cooling water on exit from the compressor, dependent upon its
temperature. If the temperature is low, flow is directed back to the pump
inlet without being cooled. If the temperature is high, it is directed to the
cooling tower.
4. If compressors of the same type and design are used, the following
advantages are gained:
• maintenance personnel become familiar with the machines
• the amount of spares held in stock are minimised because of
interchangeability.
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5. The main advantage water cooling possesses over air cooling is the fact
that water cooling gives greater control and stability of temperature.
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________________________________________________________________________________________
SUMMARY ________________________________________________________________________________________
The correct selection of a compressor for any given situation entails an
understanding of quite a number of variables. Coupled with the information
given in the previous three lessons, a clear picture should now be emerging.
Given below are the major factors to be considered when selecting a
compressor:
• the working pressure required, which is determined by plant usage
• the capacity requirement of the system – this is obtained by adding
together the requirements of each piece of equipment, and making
allowances for leakage and future expansion
• the quality of the air required, including permissible levels of moisture
and oil
• the kind of duty to which the compressor is going to be subjected
• financial considerations
• installation costs – these are higher if special buildings, soundproofing or
foundations are required
• the type of prime mover required
• maintenance considerations.
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setdistillerparams << /HWResolution [2400 2400] /PageSize [612.000 792.000] >> setpagedevice