Compressed Air Systems – click the questions below to go the answers

Q. My air compressor seems to turn on and off frequently. Is this an indication of an upcoming failure or some other matter?
The Pro Says: The relationship of the amount of compressed air you need to the amount you produce is important. There are a few factors to consider.
If your compressor is oversized for the air demand and the type of control on the machine is (load/no load) then compressor will CYCLE. Cycling is when the compressor responds to an air demand and then either shuts off or unloads. If the volume delivered is much greater than the need, the compressor is continually starting and stopping (CYCLING).
Most compressors with (load/no load) control are equipped with a timer that can be adjusted to allow the compressor to idle rather than turn off, reducing the high demand on frequently starting and stopping the motor.
Another important point to consider is the size and location of your air receiver tank, A general rule of thumb for (load/no load) controls is 5-gallon tank capacity for every horsepower, i.e. 50 HP For a 250-gallon tank.
Compressors equipped with modulation controls reduce the cycling effect by responding to the actual need through pressure identification. As the air demand increases, the compressor automatically provides more air volume and reduces volume as the demand declines. There are several types and styles of modulating controls, each compressor manufacturer offers different designs to accomplish the same result. The cost of operation can be a direct result of proper controls to meet your specific application.
Lastly, you may simply have too large of an air compressor to meet your needs.

Q. I'm adding about a quart of oil a week to my 100 HP rotary screw compressor, is that about average?
The Pro Says: That depends on the type, age and condition of your compressor and if you’re operating 8, 16 or 24 hours per day. Assuming your machine is 10 years old or less and you’re running 24 hours per day, that sounds about right. Most manufacturers state their oil carry-over at 2-3(PPM) parts per million.
Proper oil and filter maintenance are very important to overall longevity and oil carry-over problems. If the air/oil separator is oversaturated, it may collapse causing a considerable increase in oil carry-over. The lubricating oil in a rotary screw compressor serves three functions: 1) lubricates the bearings, 2) seals the rotary, and 3) removes the heat. If the oil level is low or old, all three of these functions are in
jeopardy.

Q. What is the most economical way to remove moisture (water) from my air system?
The Pro Says: Water removal is not as much of an economical issue, but rather an application issue.
Some air requirements can tolerate moisture without a problem while others will not and may cause end product problems and may damage production equipment. The amount of moisture in an air line is the direct result of the ambient temperature and humidity level. The higher the humidity the more water in the air line.
A refrigerated air dryer is designed to reduce the dew point down to + 38º F. This dew point feels dry to the touch and is acceptable for most industrial applications.
A desiccant dryer will typically reduce the dew point down to a -40ºF level. It can however, be adjusted anywhere from 0º F to – 100º F if required. A point to note is that desiccant dryers require purge air for operation. Depending on the design, the losses are as high as 15 to 17% of the incoming air. (Example), 500cfm incoming air saturated at 100º F and 100 psig will deliver 420cfm outlet air at (-) minus 40º F.
It’s important to know the application requirements before selecting an air dryer.

Q. What causes pressure drops?
The Pro Says: The simple answer is any obstruction or restriction in the air line. However, the size of the air pipe, the distance the air travels, the number of bends in the line and the type of accessory components used (filters, dryers, etc.), all contribute to line losses.
Frequently when plants expand they simply add more pipe to the end of the line, as well as sometimes adding a compressor. When you deliver out of the compressor at a higher pressure to compensate for line losses you are spending premium dollars. A properly designed air system with the correct compressor location and adequate pipe sizing can save as much as 20% in energy costs.

Q. I know air leaks are costly, can you give me a general rule as to how costly?
The Pro Says: A good general rule is: Based on 24 hours per day / 7 days per week operation a compressed air system operation at 100 psig with a cost of power at $0.05 per kilowatt-hour with (one) 1/4" size opening will waste $8,382.00 annually. A 1/4" opening at 100psig will lose approximately 100cfm or 25 horsepower of air.

Q. What is the difference between cfm (cubic feet per minute) and acfm (actual cubic feet per minute)?
The Pro Says: cfm free air is air delivered to a certain point at a certain condition, converted back to ambient conditions. acfm is the flow rate of air at a certain point at a certain condition at that point.

Q. How can we determine the cost of air at our plant?
The Pro Says: A recent survey by the U.S. Department of Energy indicated that for a typical industrial facility, approximately 10% of the electricity consumed is used to generate compressed air. For some facilities, compressed air generation may account for 30% or more of the electricity consumed.
Compressed air is an on-site generated utility. Very often, the cost of generation is not known; however, some companies use a value of 18-30 cents per 1,000 cubic feet of air. Compressed air is one of the most expensive sources of energy in a plant. The overall efficiency of a typical compressed air system can be as low as 10-15%. For example, to operate a 1 HP air motor at 100 pounds per square inch gauge (psig), approximately 7-8 HP of electrical power is supplied to the air compressor. To calculate the cost of compressed air in your facility, use the formula shown below:
| Cost ($) = |
| (bhp) x (0.746) x (# of operating hours) x ($/kWh) x (% time) x (% full-load bhp) |
|
| Motor Efficiency |
Where:
bhp—Motor full-load horsepower (frequently higher than the motor nameplate horsepower—check equipment specification)
0.746—conversion between hp and kW
Percent time—percentage of time running at this operating level
Percent full-load bhp—bhp as percentage of full-load bhp at this operating level
Motor efficiency—motor efficiency at this operating level
Example
A typical manufacturing facility has a 200 HP compressor (which requires 215 bhp) that operates for 6800 hours annually. It is fully loaded 85% of the time (motor efficiency = .95) and unloaded the rest of the time (25% full-load bhp and motor efficiency = .90). The aggregate electric rate is $0.05/kWh.
Cost when fully loaded =
(215 bhp) x (0.746) x (6800 hrs) x ($0.05/kWh) x (0.85) x (1.0) = $48,792 .95
Cost when unloaded =
(215 bhp) x (0.746) x (6800 hrs) x ($0.05/kWh) x (0.15) x (0.25) = $2,272 .90
Annual energy cost = $48,792 + $2,272 = $51,064

Compressed Air System Control Strategies
Improving and maintaining compressed air system performance requires not only addressing individual components, but also analyzing both the supply and demand sides of the system and how they interact, especially during periods of peak demand. This practice is often referred to as taking a systems approach because the focus is shifted away from components to total system performance.
Matching Supply with Demand
With compressed air systems, system dynamics (changes in demand over time) are especially important. Using controls, storage and demand management to effectively design a system that meets peak requirements but also operates efficiently at part-load is key to a high performance compressed air system. In many systems, compressor controls are not coordinated to meet the demand requirements, which can result in compressors operating in conflict with each other, short-cycling, or blowing off—all signs of inefficient system operation.
Individual Compressor Controls
Over the years, compressor manufacturers have developed a number of different types of control strategies. Controls such as start/stop and load/unload respond to reductions in air demand by turning the compressor off or unloading it so that it does not deliver air for periods of time. Modulating inlet and multi-step controls allow the compressor to operate at part-load and deliver a reduced amount of air during periods of reduced demand. Variable speed controls reduce the speed of the compressor in low demand periods. Compressors running at part-load are generally less efficient than when they are run at full-load.
Multiple Compressor Controls
Systems with multiple compressors should use more sophisticated controls to orchestrate compressor operation and air delivery to the system. Network controls use the on-board compressor controls’ microprocessors linked together to form a chain of communication that makes decisions to stop/start, load/unload, modulate, and vary displacement and speed. Usually, one compressor assumes the lead role with the others being subordinate to the commands from this compressor. System master controls coordinate all of the functions necessary to optimize compressed air as a utility. System master controls have many functional capabilities, including the ability to monitor and control all components in the system, as well as trending data, to enhance maintenance functions and minimize costs of operation. Most multiple compressor controls operate the appropriate number of compressors at full-load and have one compressor trimming (running at part-load) to match supply with demand.
Pressure/Flow Controllers
Pressure/Flow Controllers (P/FC) are system pressure controls that can be used in conjunction with the individual and multiple compressor controls described above. A P/FC does not directly control a compressor and is generally not part of a compressor package. A P/FC is a device that serves to separate the supply side of a compressor system from the demand side, and requires the use of storage. Controlled storage can be used to address intermittent loads, which can affect system pressure and reliability. The goal is to deliver compressed air at the lowest stable pressure to the main plant distribution system and to support transient events as much as possible with stored compressed air. In general, a highly variable demand load will require a more sophisticated control strategy to maintain stable system pressure than a consistent, steady demand load.

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