Wednesday, May 14, 2008

Are you wasting compressed air?

Potentially Inappropriate Uses of Compressed Air

Compressed air is clean, readily available, and simple to use.As a result, compressed air is often chosen for applications forwhich other energy sources are more economical. Inappropriate uses of compressed air include anyapplication that can be done more effectively or more efficiently by a method other than compressed air.

Don't WASTE your Compressed Air.
Check your facility for wasteful and perhaps even un-safe uses of compressed air.

Examples of potentially inappropriate uses of compressed air include:
• Open blowing
• Sparging
• Aspirating
• Atomizing
• Padding
• Dilute-phase transport
• Dense-phase transport
• Vacuum generation
• Personnel cooling
• Open hand-held blowguns or lances
• Diaphragm pumps
• Cabinet cooling
• Vacuum venturis.

Here's an explaination of each potentially inappropriate use and a suggested alternative:



Open Blowing


Open blowing is using compressed air applied with an open, unregulated tube, hose, or pipe for one of these applications:
• Cooling
• Bearing cooling
• Drying
• Clean-up
• Draining compressed air lines
• Clearing jams on conveyors.

The alternatives to open blowing are vast.


Some are:
• Brushes
• Brooms
• Dust collection systems
• Non-air-loss auto drains
• Blowers
• Blowers with knives
• Electric fans
• Electric barrel pumps
• Mixers
• Nozzles.

Sparging


Sparging is aerating, agitating, oxygenating, orpercolating liquid with compressed air. This is a particularly inappropriate application because liquid can be wicked into a dry gas, increasing the dew point.The lower the dew point of the compressed air, the more severe the wicking effect. This can occur with oil, caustics, water rinse materials, etc.
Alternatives to sparging include low-pressure blowers and mixers.

Aspirating
Aspirating is using compressed air to induce the flow of another gas with compressed air such as flue gas.
An alternative is a low-pressure blower.

Atomizing
Atomizing is the use of compressed air to disperseor deliver a liquid to a process as an aerosol. Anexample is atomizing fuel into a boiler. Fluctuating pressure can affect combustion efficiency.
An alternative is a low-pressure blower.

Padding
Padding is using compressed air to transport liquids and light solids. Air is dispensed over the material to be moved. The expansion of the air moves the material. The material is usually only moved short distances. An example is unloading tanks or tank cars. Molecular diffusion and wicking are typical problems with padding.
An alternative is low to medium pressure blowers.

Dilute-Phase Transport
Dilute-phase transport is used in transporting solids, such as powdery material, in a diluted format with compressed air. Molecular diffusion and wicking are typical problems with dilute phase transport.
An alternative is a low- or high-pressure blower or a low pressure air compressor designed for 35 psig. The pressure required depends upon the moisture content and size of the material being transported.

Dense-Phase Transport
Dense-phase transport is used to transport solids in a batch format. This usually involves weighing a batch in a transport vessel, padding the vessel with compressed air, forcing the batch into a transport line, and moving it in an initial plug with a boost o fcompressed air at the beginning of the transport pipe.Once the material is moving in a plug, the operation may fluidize the material in a semi-dense or moderate dilute-phase using fluidizers or booster nozzles along the transport path. The material is typically transported to a holding vessel that dispenses it on an as-needed basis using pad air from the secondary transport vessel to move it to the use location. A typical application would be the dense-phase transport of carbon black.

There are typically four compressed air elements to the transport. These elements are control air for the equipment, pad air for the initial transporter, transport air to move it in the piping, and fluidizers or booster nozzles along the transport piping. Most dense-phase manufacturers specify 80 to 90 psig with one singlel ine supporting the entire process. The control air and booster nozzles typically use pressures in the 60 to70 psig range. The actual article psig required for the pad air and the transport air is typically 30 to 45 psig. Because of the lack of storage in most of these applications and the high-volume, short-cycle transport times, the original equipment manufacturers request 80 to 90 psig and use the entire supply system as the storage tank. As this usually has a negative impact onthe plant air system, separate compressors, filters, and dryers are applied to this process at the elevated pressure.

Alternatives include supporting the control air,pad air, and boosters with regulated plant air plusmetered storage, and using a two-stage, positivedisplacementblower (28 psig) or single-stage compressor(40 to 50 psig) for the transport air. Another alternativeis to use metered storage for both the pad air andtransport cycle. This necessitates providing the entirer equirement from storage and metered recovery percycle, with a metering adjustment to refill the vessel just before the next transport cycle. The storage should be sized to displace the required air first for the padand then for the transport cycles within an allowable pressure drop to terminate the transport cycle pressureat the required article pressure. This will flatten the volumetric load on the system, eliminate any impacton other users, and reduce the peak energy required to support the process.

Vacuum Generation
The term vacuum generation describes applications where compressed air is used in conjunction with aventuri, eductor, or ejector to generate a negative pressuremass flow. Typical applications are hold-downs or 55-gallon, drum-mounted, compressed air vacuum cleaners. This is by far the most inefficient applicationin industry with less than 4 percent total efficiency, although for very intermittent use (less than 30 percentload factor), compressed air can be a reasonably efficient solution.
An alternative is a vacuum pump. If a compressed-air-generated vacuum is required, install a solenoid valve on the compressed air supply line to shut this application off when it is not needed. Vacuum generators are used throughout industry.

Some applications for vacuum generators include:
• Shop vacuums
• Drum pumps
• Palletizers
• Depalletizers
• Box makers
• Packaging equipment
• Automatic die-cutting equipment.

Vacuum generators are selected for safety, ease of installation, physical size of the generator, the fact that no electricity is required at the point-of-use, and low first cost. Vacuum generators are usually less economical to operate than central vacuum systems.

As a rule, in a base load situation, if the vacuum generator is operating less than 30 percent of the time,it will be more economical to operate than a central vacuum system. Otherwise, vacuum generators are, in general, less effective at pulling a vacuum and cost as much as five times more to operate than a dedicated vacuum pump. Using vacuum generators for shop vacuums and drum pumps, which are typically peak load applications, could cause another compressor to turn on and stay on until it times out. Having to operate a second compressor because of the added demand associated with a vacuum generator eliminates any apparent savings associated with a vacuum generator, even if it operates only once a day for a short period of time.

A dedicated vacuum pump, or the use of central vacuum system will provide more suction force at a fraction of the cost of vacuum produced by compressed air. In this case, it is significantly more cost effective to provide a system that is designed into the machine from the beginning than to retrofit a piece of equipment.This can be accomplished by being proactive at the time the machine specifications are prepared and the purchase orders issued. Vacuum generators must be applied properly and only after taking life cyclecosts into consideration.

Vacuum venturis are a common form for vacuum generation with compressed air systems. In a venturi system, compressed air is forced through a conical nozzle. Its velocity increases and a decrease in pressure occurs. This principle, discovered by 18th century physicist G. B. Venturi, can be used to generate vacuum without a single moving part.

Multi-stage venturi devices provide a more efficient ratio of vacuum flow to compressed airconsumed than single-stage venturi devices. Where vacuum requirements vary significantly, or are cyclical with a duty cycle of less than 30 percent, multi-stage,venturi-type vacuum generators with pressure regulators and automatic shut-off controls on the compressed air supply may be more efficient than continuously operating mechanical-vacuum pump systems. These devices also can be equipped with a vacuum switch that signals a solenoid valve to shut off the air supply when a set vacuum level is attained, thus reducing air consumption in non-porous applications. They may also be suitable where it is impractical to have a central vacuum system, particularly where the uses may not be confined to one area.

Personnel Cooling
Personnel cooling is when operators direct compressed air onto themselves for ventilation. This is dangerous because it can shoot particulates into the skin. A 1/4-inch tube blowing air on an operator can consume 15 to 25 brake horsepower (bhp) of compressed air.
An alternative is fractional horsepower fans of 1/4 bhp or less.

Open Hand-Held Blowguns or Lances
Unregulated hand-held blowing is not only a violation of most health and safety codes, but is also very dangerous. Hand-held blowguns that conform to all occupational health and safety standards should be used.

There are different styles of blowguns that candeliver various airflows, velocities, and concentrations.The proper gun must be selected for each application. Pipes installed in the end of hose and unregulated non-approved guns must not be used. Blowguns must have no more than 30 psig discharge nozzle pressure.The nozzle should be constructed to relieve back pressure if the nozzle is plugged or blocked. The blowgun must also have a spring-operated throttle mechanism so it shuts off automatically if it is dropped.

Diaphragm Pumps
A common error is to not size diaphragm pumpsf or the maximum viscosity, highest pressure, and highest volume required. The result is poor performance and an increased supply pressure requirement.
Diaphragm pumps are commonly found installed without regulators and speed control valves. Those diaphragm pumps that are installed with regulators are found with the regulators adjusted higher than necessary. This is often because of undersized regulators and supply piping or hose. The higher-than-necessary setting of the regulator increases the demand on the compressed air system and increases operating costs.With a higher pressure setting, the amount of compressed air admitted into the diaphragm chamber is increased above that which is actually required tomove the product. The amount of product actually transferred remains the same, but the amount of air used increases with the increased pressure.

The regulator should be adjusted to equal the maximum head that the pump is required to provide.A flow control valve installed up stream of the regulato rwill accomplish the required speed control. Operating the diaphragm pump without speed control increases the rate of compressed air consumption by increasing the strokes per minute of the diaphragm pump. The speed control should be adjusted to pump product in the maximum allowable time. As a general rule, the regulator and flow control valve are not included with the standard pump package. Also, when the pump has no liquid or slurry to pump, it will rapid cycle, wearing out the diaphragm and wasting air. The pump controls must be configured to turn the pump off when there is nothing to pump.

Cabinet Cooling
Cabinet cooling should not be confused with panel purging. The following are typical applications where cabinet cooling is found.
• Programmable controllers
• Line control cabinets
• Motor control centers
• Relay panels
• Numerical control systems
• Modular control centers
• Computer cabinets.

When first cost is the driving factor, open tubes, air bars (copper tube with holes drilled long the lengthof the tube) and vortex tube coolers are often used to cool cabinets. When life-cycle costs are taken into consideration, these choices prove to be expensive. It is not uncommon to find an open tube or air bar consuming 7-1/2 horsepower (hp) of compressed air to cool a cabinet. Vortex tube coolers can be an improvement over open tubes and air bars because they areoften cycled with a thermostat control, which reduces air consumption. However, air to air, air to water and refrigerated cabinet coolers are available that only use1/3 hp to accomplish the same task.

Other Potentially Inappropriate Uses
Other improper uses of compressed air are unregulated end uses and those that supply air to abandoned equipment, both of which are described below.

Unregulated End Uses
A pressure regulator is used to limit maximum end use pressure and is placed in the distribution system just prior to the end use. If an end use operates without a regulator, it uses full system pressure. This results in increased system air demand and energy use, since the end use is using air at this higher pressure. High pressure levels can also increase equipment wear, resulting in higher maintenance costs and shorter end use equipment life.

Abandoned Equipment
Many plants undergo numerous equipment configuration changes over time. In some cases, plant equipment is no longer used. Air flow to this unused equipment should be stopped, preferably as far back inthe distribution system as possible without affecting operating equipment.

Using Compressed Air
As a general rule, compressed air should only be used if safety enhancements, significant productivity gains, or labor reductions will result. If compressed air is used for an application, the amount of air used should be the minimum necessary - quantity and pressure and should be used for the shortest possible duration.

Compressed air use should also be constantly monitored and re-evaluated.

www.IndustrialAirCompressors.biz
Owned and Operated by
Tommy McGuireMcGuire Air Compressors, Inc.
“Real People with Real Air Compressor Experience”
Email:
compressors@mcguire.biz
1-888-229-9999

Wednesday, May 7, 2008

How to Minimize Pressure Drops in your Compressed Air System

Ask a Question:
What causes pressure drop in my compressed air system?

Answer:
Any type of obstruction, restriction, or roughness in the system will cause resistance to air flow and cause pressure drop.

In the distribution system, the highest pressure drops usually are found at the points-of-use, including undersized or leaking hoses, tubes, disconnects, filters, regulators and lubricators (FRLs).

On the supply side of the system, air/lubricant separators, aftercoolers, moisture separators, dryers and filters can be the main items causing significant pressure drops. The maximum pressure drop from the supply side to the points-of-use will occur when the compressed air flow rate and temperature are highest.

Your Compressed Air System components should be selected based upon these conditions and the manufacturer of each component should be requested to supply pressure drop information under these conditions. When selecting filters, remember that they will get dirty. Dirt loading characteristics are also important selection criteria.

Large end users who purchase substantial quantities of components should work with their suppliers to ensure that products meet the desired specifications for differential pressure and other characteristics.

The distribution piping system often is diagnosed as having excess pressure drop because a point-of-use pressure regulator cannot sustain the required downstream pressure. If such a regulator is set at 85 psig and the regulator and/or the upstream filter has a pressure drop of 20 psi, the system upstream of the filter and regulator would have to maintain at least 105 psig. The 20 psi pressure drop may be blamed on the system piping rather than on the components at fault. The correct diagnosis requires pressure measurements at different points in the system to identify the component(s) causing the excess pressure drop. In this case, the filter element should be replaced or the filter regulator size needs to be increased, not the piping.

How to Minimize Pressure Drop
Minimizing pressure drop requires a “systems approach” in design and maintenance of the system. Air treatment components, such as aftercoolers, moisture separators, dryers, and filters, should be selected with the lowest possible pressure drop at specified maximum operating conditions. When installed, the recommended maintenance procedures should be followed and documented.

Additional ways to minimize pressure drop are as follows:
• Properly design the distribution system.
• Operate and maintain air filtering and drying equipment to reduce the effects of moisture, such as pipe corrosion.
• Select aftercoolers, separators, dryers and filters having the lowest possible pressure drop for the rated conditions.
• Reduce the distance the air travels through the distribution system.
• Specify pressure regulators, lubricators, hoses, and connections having the best performance characteristics at the lowest pressure differential. These components must be sized based upon the actual rate of flow and not the average rate of flow.

*SOURCE: Improving Compressed Air System Performance: A Sourcebook for Industry is a cooperative effort of the U.S. Department of Energy’s Office of Energy Efficiency and Renewable Energy (EERE) Best Practices and the Compressed Air Challenge®.

www.IndustrialAirCompressors.biz
Owned and Operated byTommy McGuire
McGuire Air Compressors, Inc.
“Real People with Real Air Compressor Experience”
Email: compressors@mcguire.biz
1-888-229-9999

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