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The
Business
of
Compressed
Air
Presented at the Central Florida Section of AIChE Annual
Meeting
by
Robert B. Laine II
Clearwater,
FL June 5, 2004 |
Why should there be any
interest in your compressed air system? Operating cost is the
reason. Compressed air is the most poorly designed and managed of
all the industrial utility systems. There is enormous opportunity
to reduce operating cost ranging from 25 to 40% and additionally, to
improve the quality of the air that frequently negatively affects
performance of most, if not all, of the air consuming equipment in
the plant. One might immediately ask how any facility could have
such a large opportunity.
We frequently find
systems that were originally designed with a single compressor where
the compressor was significantly larger than the actual demand and a
spare purchased of similar size. After a year or two of operation,
both compressors are operating all the time because of a single
event that happens once or twice a year where the pressure decays
beyond an acceptable level. As plants increase in size, the next
compressor added is more often than not the same as the first two
because of ease of maintenance with no knowledge of whether the
compressor is appropriate for the system or operating cost. As the
facility continues to grow, a portion of the plant has an
insufficient pressure problem, which is solved by adding another
compressor room in the general vicinity of the symptom with no idea
of what the actual problem is. Most plants have no idea how much
demand they have other than the total of the “on” compressors. An
“on” compressor is not an indication of need or that it is actually
compressing any air into the system. Compressed air is the last
issue engineered for a new plant or expansion and frequently the
design agenda is to make sure there is enough or “more is better.”
Compressed air is the
most expensive of all utilities, for the amount of work derived from
the energy input to the compressor motor and clean up equipment.
Eighty-five percent of the electrical energy is dissipated as heat
and another 4% is lost when the air is cleaned up and distributed to
your customers, which leaves 11% to perform work. And this only if
the system is very efficient. It is not at all unusual for systems
to be less than 5% efficient once all the part loaded compressors,
poor applications, artificial demand, drainage, and leaks are
identified.
More often than not,
there is very little understanding of the working relationship of
the different components within the supply side of the compressed
air system. What type of compressors are required; recip,
centrifugal, contact cooled rotary screw, or dry screw? Will
different types of compressors work in the same system? Is one
design more efficient than another and what is the most appropriate
size for my facility? How many compressors are needed and what is
the intensity of maintenance? What about variable frequency
drives? Is one large compressor better or worse than several
smaller ones and how is the risk of interruption defined and what
provisions are made to prevent interruption? All compressors are
rotating equipment and will fail. It is not “if,” but “when.” What
dryers do we purchase; desiccant, non-cycling refrigerant, cycling
thermal mass refrigerant, or externally heated blower purge
desiccant? What is instrument quality air and how do we obtain it?
Do we need instrument quality air? Is filtration necessary? What
efficiency is required and where in the system should the filtration
be located? Most compressed air purchasing decisions are based on
capital cost, as there is little knowledge of the “system” to make
purchasing decisions on any issue other than price.
Often the different
departments within the plant will have totally different agendas for
compressed air. Production wants “all that they want” and it must
be instrument quality as defined by the Instrument Society of
America, but want nothing to do with how it is generated, how much
they waste, or what it costs. Maintenance wants a system that is
dependable with minimum effort that never fails. Maintenance may
evaluate system performance based on the number of complaints from
production concerning pressure and if there are no complaints, the
system must be pretty good. Systems where there are no complaints
and operating personnel feel the quality is good most often present
the greatest opportunities to reduce operating cost. Plant
management wants nothing to do with compressed air as long as no one
complains and compressed air never interrupts production.
Accounting wants minimum cost regardless of whether the system is
maintained properly. Frequently, the different departments do not
discuss or communicate with one another about compressed air as long
as there is enough. “More is better.”
Why is the system
contaminated with water and oil, when there are functional dryers
and filters in the system? How do we tell if the compressed air
system is working well? If there are no complaints, are we doing a
good job? This and those above are just a few of the questions that
we are asked when providing an audit.
One of the issues about
compressed air that is always true is the use of “absolute” words.
Notice the word “always” in the preceding sentence. Sooner or
later, the use of an absolute word in reference to compressed air
will be wrong. Compressed air is very dynamic and variable and
since it is a compressible fluid, it does not behave the same as
other non-compressible fluids. Flow direction arrows on compressed
air piping will not always be correct, especially when trying to
analyze an existing system. One area where we are confident of
issue is the “more is better” statement. There is nothing about
compressed air where “more is better” other than storage. And even
here, the storage must be with tanks, not in the piping.
What does this auditor define as the perfect system?
The pressure must be constant for all operating
conditions at ± some value (0.5-psi for example) and the air must be
clean and dry if used for actuation, instruments or any other
application that is sensitive to water and/or oil if the compressors
are lubricated. Dryness depends on the system and how the air is
used. Clean, dry, and free of all liquids absolute for all
operating conditions is a more than satisfactory statement of
dryness for most systems. This system will not have a pressure dew
point below 0 °F, which is a common requirement for instrument
quality air. However, some systems and processes are sensitive to
moisture as a contaminant such as computer chip manufacturing where
moisture is absorbed by the silicone chip, which is unacceptable.
Pressure dew point for chip manufacturers will be near minus 100
°F.
All “on” compressors must be base loaded (operating at
100% of volume at design pressure) except for one compressor that
provides trim.
System efficiency is expressed as standard cubic feet
per brake horsepower (scf/bhp) not at the compressor inlet or
discharge, but at the point of use. Purchasing efficient
compressors for an inefficient system is a poor business decision.
What
is an audit, what can it do for me, what will I receive, what can I do
with the final report, and what does it cost?
An audit consists of a thorough analysis of the supply
side of the system including but not limited to the following. The
amount of air being compressed and the pressure fluctuations and what
causes the pressure fluctuations. The amount of waste in the compressor
room; part loaded compressors, compressor blow off, drainage, artificial
demand, leaks, etc. The total power of supply including dryers with a
calculated efficiency, compressor by compressor expressed as scf/bhp or
kW. What is the quality of the air with a detailed explanation of why
there is water and/or oil in the system with functional clean up
equipment?
The distribution system will be evaluated for
differential and the ability to deliver the air to the most distant
point in the system. Pipe size will be evaluated and discussions of
closed loops and whether or not additional piping has any benefit
evaluated. Old carbon steel piping will be evaluated for contamination
source and risk of failure.
Storage will be evaluated for size and location.
Additional storage will be recommended, designed and located with
detailed explanation of how to best implement storage. There are four
different types of storage that may offer opportunities. Control
storage, which is located on the supply side of the system; general
storage, which can be anywhere in the demand side of the system;
dedicated storage for one specific application; and high pressure
off-line storage that is sometimes referred to as load shaping.
The demand side of the system is also evaluated for
poor application of compressed air that may have an alternate source of
energy (low pressure blowing for example) that is less expensive with an
attractive return to install the low pressure blowing system versus
using regulated high pressure compressed air. Specific recommendations
are provided to modify the demand side use of compressed air with the
savings opportunity defined comparing the existing with proposed
operating costs with a calculated return of investment. Most systems
will have about half the savings opportunity on the demand side of the
system.
Drawings will include
an existing process flow diagram and a proposed system arrangement plus
any detail of demand side issues that are necessary to modify point of
use applications or a change of energy source. Specific recommendations
are provided for modification of supply to improve efficiency and to
clean up the compressed air. The same is also provided for demand side
opportunities with enough detail that project engineering can implement
those recommendations.
An Excel spread sheet is provided detailing all the
financials of the existing system and proposed system with an action
plan including capital and installation costs for all recommended
equipment or systems. A calculated return of investment is provided
including the cost of the audit as a line item. Most plant wide audits
can be accomplished four to five days on site. Firm pricing for the
audit can be provided once the type and number of compressors are known,
the number of entry points into the system, and the type of dryers are
provided to the auditor. General estimates of savings potentials can be
provided with the audit quotation.
An out briefing is provided at the end of the on site
portion of the audit to provide the details of all recommendations that
permit plant personnel the opportunity to ask questions discuss the
recommendations while the auditor is still on site. The entire audit is
a learning process where we educate as many plant personnel as possible
about compressed air systems. Or only goal is to better educate the
plant about compressed air systems.
Robert B. Laine II is
President of Southern Corporation of South Carolina and a Senior Auditor
for Plant Air Technology. For the last 10-years he has participated
exclusively in auditing more than 250 compressed air systems in the
Americas for many small and Fortune 500 companies from Abbott Labs to Y
& S Candies (part of Hershey Foods). Robert (Bob) has no financial
interest in the audit solution and does not sell or receive commission
for any sales of equipment associated with compressed air systems.
Please feel free to visit the Southern Corporation web site:
compressedairauditing.com
or contact him at
bobbysc@aol.com . As a former manufacturer’s agent, he sold
chemical process equipment to the phosphate industry in Florida and is
familiar with the processes of both sulphuric and phosphoric acid.
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