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Thursday, April 29, 2010

How to Install and Adjust a Pneumatic Storm Door Closer

Storm doors are hung on the frame of an exterior door. A storm door typically has a screen and glass insert that are interchangeable based on the weather needs. A pneumatic door closer can be used to automatically pull the storm door closed, to control how far the door can open and to brace the door open. A pneumatic store door closer may come with the storm door or may be purchased separately. Installing a pneumatic storm door closer should take less than one hour.

Step 1

Make sure the storm door opens and closes properly before installing the door closer. If installing a replacement storm door closer, then remove the old closer.

Step 2

Choose a location on the top or middle of the storm where you want to install the door closer. Top mounted can insure that a young child will not get their hands pinched in the closer. If replacing an old door closer, you may want to install the new closer at the same location. If the closer package came with a paper template, secure the template using the manufacturer's instructions.

Step 3

Hold the assembled, compressed storm door closer to position it with the screw mount bracket on the door and the square door jamb (frame of the door) bracket in about the center of the jamb. There should be at least enough space above a top-mounted closer for you to fit a finger between the closer and the top door frame. At the point, the unit does not have to be perfectly level; just eye-ball it for level. The objective is to determine where the door mount bracket should be.

Step 4

Mark the holes in the screw mounts of the door portion only. For ease of installation, pull the pin that holds the bracket to the closer. Pre-drill the holes on the door mount, taking care to not go completely through door. Attach the bracket to the door with the included screws. Re-attach the pump to the bracket.

Step 5

Position the door closer end to the door jamb while the storm door is closed. Place a level on top of the closer to ensure it is level and then use the pen to mark the holes for the screws. Pull the pin that holds the bracket to the closer.

Step 6

Drill the holes in the door frame and secure the closer with the screws. Re-attach the pin connecting the closer to the door jamb bracket.

Step 7

Adjust the speed at which the pneumatic door closes by twisting by hand or with a screwdriver (depending on the unit purchased) the knob/screw located on the door end of the closer. A clockwise turn slows the closer; counterclockwise speeds up the rate of closing.

Wednesday, April 28, 2010

Troubleshooting Your Pneumatic Golf Cart Motor

The job of a usual golf cart motor is to convert electrical energy so that your golf cart can move. Most of the time, it uses the concept of magnetism to simultaneously attract and repel the parts in order for the shafts to move. Pneumatic motors use the same concept but it uses compressed air and transforms it to energy that can power mechanical work. Pneumatic motors are not as efficient as the usual motors, which is why there are a number of problems that one can encounter with a golf cart that uses pneumatic motors. You can easily troubleshoot pneumatic motor problems.

Overheating

Overheating is a common problem of any kind of motor. This is because the rotating mechanism produces heat inside the device. If the heat inside accumulates and the system is not able to dissipate the temperature properly, then it can lead to overheating. The problem of overheating can be attributed to the parts of the motor that keeps rubbing into each other which causes the increase in heat. In order for you to solve this problem you should lubricate the motor. There are oil holes in different parts of the motor which you have to place a few drops of oil. A common symptom of an overheated motor is when you smell something burnt from the device.

Wobbly Shaft

Misaligned moving parts make the shafts of your motor wobbly. This can be easily fixed by opening your motor, inspecting the shaft and making the necessary modifications. If the shaft is misaligned, screw out the shaft and position it properly. If the shaft is wobbly because it is not secured properly into the motor, then simply screw the shaft tighter.

Sparks in the Motor

The most dangerous kind of problem that you might encounter involves the presence of sparks inside your motor. This is often caused by rotor, stator and brushes that are damaged. To solve this problem, open your motor and inspect the rotor, stator and brushes to find out if any of them is damaged. Replace the damaged ones by following the instructions in your manual. Seeing sparks inside your motor must signal that you need to urgently pay attention to your motor. You do not want any other part of your motor to catch fire.

Motor Is Too Hot

A pneumatic motor, just like any other kind of motor, is designed so that there is proper ventilation for the heat that the device accumulates throughout its use. The most usual reason why your motor is too hot to touch is because the heat is trapped inside the device. This should not be the case because heat has to always flow out of the vent holes. But if the holes are covered, the heat is contained within the system. To solve this problem, visually inspect the motor and see if there is any part of the cart that is blocking the vent holes and reassemble the parts so that the vent holes are left open.

Monday, April 26, 2010

Electric Needle Gun vs Pneumatic Needle Gun

A needle gun, or as it is also called a pneumatic needle-gun scaler, is a very useful tool to have around the house. More often than not, it is used to all of your projects that involve some sort of metalwork. This can range from all your around the house repairs and even stretching to the work that needs to be done on your motor vehicles.

In essence these types of tools are used to remove the rust and old paint that may be still sitting on any metal surfaces. Now while there are numerous needle guns to choose from, you will find that there are two types that you should consider: electric and pneumatic.

Electric Needle Guns

The basic function of a needle gun is to remove paint and rust. Electric needle guns come with a set of incredibly fine needles. The tool itself uses an electrical current to rotate these needles at varying speeds against the metallic surface to slowly chip away at the numerous layers of paint or rust that are present. Using electric needle guns are beneficial in that it makes it easier for you to do work that is around the house itself. By using a battery-operated gun, you can travel around the home quickly and more efficiently, getting into all the tiny nooks and crannies that you find.

A downfall to using an electric gun is that eventually your batteries are going to run out. A second downfall to using electric needle guns is that you cannot run the tool for a continuous period of time. Because these guns are electric, they are made of up numerous pieces. This quickly causes over heating and easily malfunctions when a single piece of it breaks. The final downfall to using electrical needle guns is that the overall cost is going to be much more expensive in the long run. You will find that you have to constantly replace pieces with the guns and that there is going to cost you much more money at the end of the day than buying a pneumatic gun.

Pneumatic Needle Guns

Needle guns are the best choice when it comes to removing rust and paint because they are able to quickly adjust to objects that are misshapen or irregular. Needle guns can strip and area clean in a matter of seconds. More often than not, you are going to find your needle guns in their pneumatic form. This refers to the fact that they are powered by compressed air.

These units used compressed air to force a piston to move backwards and forwards. It is due to this that the needles will work against your metal surfaces. These types of guns are used for garage work. This is the type of gun you are going to want to purchase when you are doing work on your cars. You are going to have to buy an air compressor in order to make sure that the gun functions properly.

One benefit of this method is you are going to have a constant source of power and you won’t run the risk of having your tools die on you while you are working. Pneumatic needle guns offer you the opportunity to easily change the torque limitations without running into any issues. Another benefit to using pneumatic needle guns is that they are very reliable in their durability.

Saturday, April 24, 2010

The Pneumatic vs Electronic Impact Wrench: Which Suits Your Needs

An impact wrench is a tool that is used in all sorts of work, especially automotive work. However, there are many reasons why the average do-it-yourselfer may need an impact wrench. If you are working with wood and building a deck or any sort of structure, an impact wrench will definitely come in handy. Impact wrenches are most commonly found in the pneumatic version.

This means that the impact provided by the wrench is powered by compressed air. There are impact wrenches that are powered by electricity. It is hotly debated which of the two impact wrenches is best, however, you should decide which one works best for you.

The Professional Choice

The pneumatic impact wrench is considered the professional grade impact wrench. It is also the wrench chosen by do-it-yourselfers that work with automobiles. This is because the compressed air provides more torque than can be produced by the electric models. However, most do-it-yourselfer are going to find that they don’t need such a high level tool for the jobs that they want completed around their home.

Higher Torque

It has been established that the pneumatic impact wrench is going to provide more torque. What does that really mean? It mean that’s the impact wrench powered by compressed air is going to provide more power with every impact. While this can be very important, the average do-it-yourselfer is not going to need super powered torque for the odd jobs that they will be completing. In exchange for the higher torque of the pneumatic impact wrench, the electric model is not going to require the use of an air compressor. This makes the electric wrench much more convenient to use and it means that it can be used in situations where an air compressor many not be available, such as changing tires on the side of the road.

Easier to Use

The pneumatic impact wrench is going to be easier on your body. It is lighter in weight and usually smaller to hold in your hand. This is because much of the power source is going to be housed in the air compressor. The electric impact wrench is going to house all of the necessary equipment inside the wrench itself and therefore, it is heavier and bulkier. Because the electric impact wrench is going to be heavier and larger, you may find that is can cause fatigue when using it for long periods of time.

Price

Impact wrenches, both pneumatic and electric, are found at a variety of price points. You can buy one for $50 or $250. It is advised that with any power tool, you don’t buy the cheapest model. This is exceptionally important if you are selecting an electric impact wrench. Because electric impact wrenches are going to be run off of battery, you want to make sure that the battery is high powered and long lasting. The best battery available today is the Lithium Ion battery. These batteries are lighter weight and long lasting. However, they are the most expensive of any battery, therefore they can increase the cost of your pneumatic impact wrench.

There you have it. Using the above information you can determine which type of pneumatic impact wrench is going to best suit your needs.

Friday, April 23, 2010

Pneumatic Fittings Filter Replacement Routines

Do you know how effective your pneumatic fittings filter is or when to change it? Right now gauging system performance is a hit or miss activity. Use of a NeSSI-bus-enabled differential-pressure or moisture-breakthrough sensor (common in continuous emission monitoring systems) would give hard data.

It would allow us to validate filter performance and move from preventive to predictive maintenance. Automation of the filter also will lead to adoption of more-intelligent filtration devices that predict life span and initiate self-cleaning routines.

Using the DCS to control analytical systems. The advent of low-cost miniature computing and control devices will enable sampling-system control functions to become distributed and local to the sample system. Simple programmable control applets will dominate, be interchangeable across platforms and available from third parties. Sensors and actuators associated with auxiliary systems such as carrier-gas generators, heat tracers, conditioners (vaporizing regulators, sample recovery systems, etc.) can be integrated on the NeSSI-bus. With these sensors we can monitor and apply set points to our auxiliary process-analytical support system. The process analytical SAM can significantly extend limited control functionality previously provided by the DCS and various controllers.

Thermostats for temperature control. We can replace thermostats with PID control loops. We already are doing this using commercially available smart heaters. Advantages include the ability to maintain higher temperatures thanks to tighter control of the heater. Although an explosion-proof heater can't run on intrinsically safe power, its temperature and set-point signals can be integrated into the NeSSI-bus. Reliability will be enhanced by being able to better monitor and control critical dew points and bubble points of the process sample.

Valve Control Module and

Transmitter: Module (left) comes with

a lockout to prevent actuation of

multiple valves at the same time.

Photo courtesy of Swagelok.

Gas cylinders for calibration and validation. More-precise flow and temperature control in a sample system affords the opportunity to opt for more permeation generators to calibrate and validate analytical sensors. Today we use bulky gas cylinders to do this chore. It would be a tremendous advantage from an installation and operational point of view to eliminate calibration cylinders when the components needed are available as permeation sources.

Maintenance resources and routine rounds.NeSSI can eliminate the need for continual checks and adjustments. The new generation of smart analyzers such as gas chromatographs will have visualization built into the sample system as part of their local human machine interface (HMI) and remote workstations, helping analyzer technicians properly troubleshoot. Indeed, troubleshooting will become more of a science than an art. Portable zone-2-rated laptop computers or PDAs can effectively serve as the new "adjustable wrench" for the technician.

Block and vent valves for gas chromatograph sample introduction. Typically to ensure constant molecular volume we reference the sample pressure to atmosphere using a block-and-vent-valve arrangement prior to injecting a sample into a gas chromatograph. The ability to use an absolute pressure sensor will allow more-precise measurement and better control without the need for block-and-vent hardware. Of course, this would require the sample system to communicate with the gas chromatograph.

System-centric health monitoring. Sensors and networking will enable expansion of monitoring to all elements of an analytical system. It will permit overall analytical system performance to appear in the control room as a traffic light status signal that tells the operator whether the complete process analytical system is good, bad or is still good but will soon require maintenance. This will improve the operator's confidence in the performance of the analyzer system.

The Path Forward

Bus systems undoubtedly will mature fairly quickly; many components including miniature flow meters, pressure sensors, smart heaters and both proportional and on/off automated valves either are available or will be in the next couple of years. Ability to purchase functional applets that could work across multiple analyzer systems will be truly revolutionary — they even may be fun to use. Today SAM functionality is embedded in more-complex analyzers such as gas chromatographs. Extending it to other analyzers demands a compact NeSSI-bus-enabled SAM.

Until that's available we'll struggle to bring standardization and simplicity to our discipline. Until then we'll continue to supply ad hoc and proprietary solutions that will work — but not support our general move to Generation III microanalytical and by-line installations. Our objective is to allow a microanalytical manufacturer to be able to plug into the mechanical and communication rails — and configure its devices sampling tasks using off-the-shelf applets. This architecture finally will enable the sampling and analytical measurement to go hand-in-hand as an integrated package.

The cost and pneumatic fittings technical effort to move to complete sample-system automation will be high. However end users will gain significant rewards including higher reliability and lower maintenance costs. It'll take a clear vision and concerted effort to change the game — but the horse is out of the barn and it's only a matter of time before we'll look back and wonder why we clung to our manual systems for so long. However, until that time comes we'll continue, out of sheer habit, to build steel copies of wooden bridges.

Wednesday, April 21, 2010

Sample Pneumatic Components System Fabrication Techniques

Size and weight do matter with NeSSI. Because our plan is to get the pneumatic equipment by-line (i.e., next to the sampling point), it's important that a system is small and light so that service can be done on a replacement basis. Today we have the ability to fabricate modular miniature systems that should be able to be assembled Lego-style by an unskilled person.

Yet in many cases we build modular systems that haven't been optimized for space or still require custom tubing work. We should aim to tightly integrate the modular system with its enclosure, to reduce size and weight, as well as eliminate custom tubing. Use of graphical indication of the flow paths certainly will overcome reluctance to use a densely populated sampling system.

Sample system design methodology. Software configurator tools available for designing NeSSI systems ultimately will expand to include the heaters, the microclimate enclosure, the wiring interconnections and the applets specified for the SAM. These tools will allow an end user to do a rapid detail design of a sample system based on company best practice and generate a detailed bill of materials and estimate.

Because the NeSSI bus is intrinsically safe, use of pre-certified components allows us to virtually self-certify our system as an entity regardless of where in the world the system is installed. The assembler or integrator now will be able to validate the automated performance and operation of the sample system as part of the check-out procedure by enabling self-checking routines available in the SAM. Contrast that to current designs where much of the detailed design is farmed out and systems are mainly checked only for mechanical operation.

Stream switching norms. For sample and calibration/validation fluid switching, we often use double-block-and-bleed stream-switching valves with bubbler systems to indicate a leak. This mandates maintenance rounds to regularly check if there's a leak at the bubbler. Use of miniature, modular close-coupled systems minimizes upswept voids; the need for double-block-and-bleed valves to reduce dead volume all of sudden becomes less important. Another reason for multiple valves has been to compensate for leaky valves that were standard fare in the "bad old days."

Early stream-select valves were ball valves with poor seating — later followed by explosion-proof solenoid valves that probably were even worse. Today we have better valves (see "Streamline Your Sampling System,"

And if they leak smart flow and pressure sensors can monitor valve performance. Use of close-coupled systems and smart sensors allows us to simplify our systems and reduce size and costs by minimizing the need for double-block-and-bleed stream-switching hardware. This also frees us from the burden of providing visual indications of leakage.

Rotameter Replacement: NeSSI-bus-enabled

unit can sense fluid flow, pressure and temperature,

and serve in Division 1/Zone 1 areas.

Photo courtesy of Circor.

Use of visual indication devices such as rotameters and pressure gauges. We're addicted to their usage because we've felt a need to "see" the process fluid. However, as glass rotameters have given way to armored versions with magnetically coupled indicators, what we're getting now is an inferential view of the flow. The new NeSSI-bus-compliant flow devices can transmit flow or pressure signals.

If you have a signal that's available on a graphical user interface you really don't need an indicator. Maybe it's time to remove the windows from our sample system enclosures and get a smaller transmitter in their place. Eliminating the rotameter also does away with an aggravating position constraint that dictates vertical positioning of the sample system.

Use of manual flow and pressure regulators. A rotameter generally comes with a needle valve, allowing manual flow adjustment by analyzer technicians. So, how can we adjust flow without a rotameter? Work is underway to supply a proportional valve coupled to a flow or pressure transmitter to give a real control loop on the sample system. This will allow us to monitor the flow using proportional-integral-derivative (PID) control and also input a set point.

Consider the great strides gas chromatograph manufacturers have made with carrier-gas pressure controls. The days of matching flows using needle valves are history. Thankfully needle valves used in the majority of process gas chromatographs have been consigned to the obsolete parts bin.

Shows a NeSSI-bus-enabled valve control module for actuating sample-system pneumatic valves as well as a NeSSI-bus-enabled pressure/temperature transmitter. The module is rated Division 1/Zone 1 and so can be mounted inside a sample system enclosure. When used with a gas chromatograph it can obviate separate pneumatic tubes between the chromatograph and the sample system. A single cable connection links the gas chromatograph to the solenoid valve control module.

Monday, April 19, 2010

Control a System Pneumatic Components

There are instances where we have used 4–20-mA analog signals to send pressure, temperature and flow signals from our sample systems to the DCS. (In NeSSI-speak, we call this generation 1.5). However this requires extensive wiring in a confined space; significant cost and effort need to go into design of cabling, intrinsically safe barriers, wiring and conduit to meet the electrical classification. In some cases as many as 30 I/O may be required to adequately monitor and control a system pneumatic components .

Intrinsically safe networks such as Foundation Fieldbus and Profibus, at least today, aren't physically capable of handling smaller devices such as sample system components and don't have the intrinsic power capability to support multiple devices without costly extensions.

Another critical barrier to automation has been lack of smaller sized devices (commensurate with the size of sample systems) such as actuators. Miniature actuators are scarce in the instrumentation field, so we haven't been able to borrow from that source. Low cost transmitters, now commonly available for instrumentation, aren't compact enough for a sampling system. The relatively smaller and fragmented market and unique technology requirements have kept the process analytical discipline from automating sooner.

The long and torturous learning process needed to develop proper extractive sampling techniques has created a very conservative mindset regarding acceptance of new technology. In addition, slow recognition of process analytical as a true discipline that crosscuts traditional engineering boundaries (instrumentation, piping, electrical) as well as functional boundaries (lab, process control, maintenance, engineering) has hindered acceptance and understanding needed to address special requirements of process analytical systems such as a purpose-built bus and local control.

The Solution

NeSSI Generation II recognized the need for a bus specific to the needs of sampling in a hazardous environment. Two variants are at hand — Siemens provides one bus, called I2C, while the other comes from CAN in Automation (CiA) (see "Intrinsically Safe NeSSI Nears," www.ChemicalProcessing.com/articles/2008/147.html) and has been adopted by ABB. Both are intrinsically safe, ultra-compact and suitable for operation in Zone 1/Division 1 environments. They also can handle as many as 20 or 30 components. (The trick is to lower the voltage to 9.5 v to allow current loads in the range of 1 amp.)

The first working examples of these buses essentially are modified extensions of on-board digital buses that have been silently operating, without a hiccup, for years inside many of our gas chromatographs. Once these buses and NeSSI-bus enabled sensors and actuators come to the marketplace, we have the tools in hand to automate our sample systems. It sounds easy but the need for different components to play nicely within a specified power budget will pose a challenge. Of course, if the sampling system isn't located in a hazardous area, the NeSSI bus can be used without an intrinsic safe power supply and associated power constraints.

NeSSI Architecture: Modular system includes

mechanical and electrical rails and can accommodate

a SAM.

Click image to enlarge.

Having a suitable bus allows us to move on two other critical issues: How do we unburden the DCS and manage our own signals? And how do we do closed-loop control and execute simple control tasks for process analytical specific requirements? We can use a NeSSI-bus-enabled local controller rated Division 2/Zone 2 (since it can be located outside of a sampling handling enclosure).

A physically large controller would defeat miniaturization efforts; we need a "hockey puck" sized programmable device that talks NeSSI-bus on one side and Ethernet or a fieldbus protocol on the other. We call this device a Sensor Actuator Manager (SAM). This SAM functionality to date has been typically embedded within smart analyzers such as gas chromatographs.

Some SAMs employ a programmable logic controller (PLC) to control a sample system. Unfortunately the sample system applets developed for these SAMs have been platform-specific and proprietary. At one CPAC workshops, attendees came up with a list of 60 applets that could provide a standard set of functions to allow a technician to set up, monitor and control a sampling system (and microanalytical device) without custom programming.

It shows the NeSSI architecture with mechanical and electrical bus rails along with a SAM. The SAM manages bus signals and controls the sample solenoid valve system via programmable applets. It also serves as an interface between a Zone 1/Division 1 NeSSI–bus handling the sample system sensors and actuators, and a higher-level communication bus. This arrangement allows plug-and-play capabilities of devices within a hazardous location.

A wireless pneumatic components personal digital assistant (PDA) or personal computer (PC) enables interaction with the SAM and provides a graphical user interface to visualize flow paths.

Friday, April 16, 2010

Rethink Sample Pneumatic System Automation

When men got structural steel, they did not use it to build steel pneumatic copies of wooden bridges," wrote Ayn Rand in her book "Atlas Shrugged." Today process sampling systems can benefit from advances due to the New Sampling/Sensor Initiative (NeSSI) — so, we should ponder whether we're really taking advantage of these innovations or just building steel copies of wooden bridges.

The Center for Process Analytical Chemistry (CPAC) at the University of Washington, Seattle, in 2000 launched NeSSI. This ambitious undertaking aimed to address reliability problems (and, yes, bad reputation) of process analytical systems. Many people associate NeSSI exclusively with the miniature mechanical footprint, adopted from an International Society of Automation (ISA) SP76 committee standard. That's Generation I, which already is well established. Today there's much more. Generation II, now under a full head of steam, automates the sample system — and sets the stage for Generation III, widespread adoption of microanalytical devices.

Automating a sample system always has been a struggle. The first continuous analyzers and their "evil" accessory, the sample system, appeared in pre-World War II Germany. Today the analyzers themselves have become modern marvels of automation. However little has changed with the sampling system. We still rely on spring and diaphragm regulators, on/off thermostats, manually adjustable needle valves and visual indicators for monitoring and control. We invariably need to do routine field checks and adjustments. Indeed, it's not unusual for analyzer technicians to make daily rounds. Process analytical has never caught up with the automation used by our instrumentation and distributed control system (DCS) associates. Sampling systems are one of the last bastions of manual operation left in a modern processing facility. Why does process analytical remain an anachronism in a sea of automation?

Development Roadmap: The ultimate

objective of NeSSI is to enable the use of

microanalytical devices.

In one company where I worked, some process automation folks called analyzers "the technology of last resort." But these folks also were part of the problem because they didn't want to handle the multiple diagnostic inputs needed to adequately monitor performance of an extensive process analytical system. Typical analyzer-to-DCS connections include component concentration signals and an analyzer fault contact (and sometimes a flow switch in parallel) to give the ubiquitous "analyzer trouble" alarm. However the majority of diagnostic elements such as sample take-off pressures, sample disposal pressures, sample flow quantities, heat-tracing temperatures used to maintain sample dew points, filter performance, calibration system check flows, analyzer shelter environmental alarms and analyzer utilities that contribute to overall analytical system reliability typically aren't monitored.

We generally remain analyzer-centric in predicting or reporting a failure to the process operator. This impacts reliability because an analyzer is only a small part (and in many cases maybe the most reliable one) of a multi-element system. To make things worse, the signals sent usually are discrete, don't predict the problem and only give an alarm when it's too late to do anything — by that time the plant may be down. When we attempt to become system-centric and send multiple signals to/from the control room, the cost of sensors, actuators, wiring and additional input/output (I/O) automation points (especially for conventional 4–20-mA signals) becomes very steep.

To make matters worse, doing closed-loop control and adding logic functions (e.g., stream switching routines) using the DCS for sample system control invokes another layer of automation that's perceived as overkill by the process automation folks. Although many sampling system automation tasks (or applets) could be standardized across the process analytical discipline, we as an industry have yet to come up with an open modular solution. So even if we get our input (and output) signals serially to the DCS, programming costs tend to ramp up because of the need for custom programming.

An Ugly Secret

Many sampling pneumatic cylinder systems handle hazardous fluids (such as hydrocarbons and hydrogen) and are packaged enclosures. Yet the electrical engineer going out to map the plot plan for electrical hazardous area ratings doesn't classify the inside of an enclosure as a Division 1/Zone 1 environment — but that's what it is. We've learned to design and package our sample systems using a potpourri of protective methods and wiring techniques to allow at least some degree of automation — e.g., explosion-proof enclosures, air solenoid valve and inert purging, hydrocarbon gas detector interlocks, equipment encapsulation, intrinsic safety, filled conduit seals, rigid conduit and armored cables. Having to meet exacting requirements of various global electrical certification agencies intensifies the problem. It's difficult and expensive to automate a sample system to meet requirements of a Division 1/Zone 1 area.

Moisture and Cold Pneumatic Air Cylinder

If product is blown into a cold pipeline, the inside surface could be wet as a result of condensation. This can occur in pipelines subject to large temperature variations, particularly where there are pipe runs outside buildings. If air drying is not normally necessary, the problem can be overcome by trace heating of exposed sections of the pipeline or by blowing the conveying air through the line to dry it out prior to introducing the pneumatic product. Lagging may be sufficient in some cases.

In normal operation, the delivery temperature of air from a Roots-type blower could be 80 Degrees C higher than the inlet temperature. This means the volumetric flow rate and the conveying air velocity will be 25 to 30 percent greater than the value at ambient temperature. On startup, the air will be relatively cold for conveying the product and, if the resulting conveying air velocity is below that necessary for the product, the pipeline could block.

Since air density increases with temperature decrease, it is essential that air requirements be based on the lowest temperatures likely. If this results in excessively high conveying air velocities during normal operation, then it will be necessary to control the air flow rate to the conveying line. Variable speed control of the air mover, choked flow nozzles in a by-pass air-supply line or discharge of air to atmosphere via a control valve could be considered.

Product in the line

If the pipeline is not purged during a plant shutdown, some product could be left in the line. On startup it's important to blow air through the pipeline before product is introduced. If the reference value of pressure drop for air blown through the pipeline is known, it can be compared with the air-purge value. If the actual pressure drop is significantly higher than the empty-line value, product may still be in the pipeline. It's also good practice to purge the line and check the pressure drop before shutdown.

Unexpected shutdown

If conveying stops unexpectedly due, for example, to a power-supply failure, it may not be possible to start the system again, particularly if there is a large vertical lift. If the bend at the bottom of the vertical section is taken out to remove the product, it may be possible to purge the line clear.

If this is a common occurrence for a plant, an air receiver can be installed between the air mover and product feeder. If the product feed into the pipeline stops at the instant the power fails, the air stored in the receiver could be sufficient to clear the line of product. Alternatively, a parallel line with valved connections to the pipeline could be fitted so that the line could be cleared slowly from the end, one section at a time.

When good systems go bad

If a system that has worked well for a long time starts to develop blockage tendencies, feeding device wear may be the cause. If air leakage across the feeding device increases, the air available for conveying the product decreases. The volumetric flow rate of remaining air may become insufficient to convey product and the pipeline will block. Worn screw flights, valve seats in gate lock valves, and rotary valve blades can all result in greater air leakage. Check these components regularly for wear and replace them when needed. Also check air movers against original manufacturers' specifications.

Keep in mind that a system that conveys one product well may be completely unable to convey another product. Minimum conveying air velocities differ from product to product, and air leakage across feeding devices is also product dependent. If a system has to convey more than one product, this requirement must be considered carefully at the design stage. Fig. 2 plots product flow rate against air flow rate for a range of products.

Long distance charges

Remember that, for any given conveying line pressure drop, the conveying capacity of a pipeline decreases as distance increases. For a change in conveying distance, therefore, there must be a corresponding change of product feed rate into the pipeline.

For a given conveying line pressure drop, the product flow rate is approximately inversely proportional to conveying distance. For a given distance, the product flow rate is approximately proportional to line pressure drop.

If the conveying distance is increased, the product flow rate will have to decrease, so product will be conveyed at a lower phase density. For a product capable of being conveyed in dense phase in a conventional system, a slightly higher conveying line inlet air velocity will be required, in turn, demanding a higher air flow rate.

If the system cannot achieve its rated duty, determine whether the problem is due to product feeding, pipeline or air supply. Check on the conveying line pressure drop. If it is below the air mover's capability, product feed into the pipeline may be insufficient. If the maximum output of the feeder does not meet the conveying capability of the pipeline, however, it will probably be necessary to fit a larger feeder.

Before recommending a larger feeder, be sure that air leakage isn't the real culprit. Check rotary valves in particular, as well as air vents and clearances on all moving parts. Don't forget to check the filtration unit. If it has been incorrectly sized, pressure drop across the filter may be too high. Also check that the filter cloths don't need replacing or cleaning. It may be that an additional or a larger filter is needed. If these modifications don't bring the system to rated output, an air mover with a higher pressure rating or an increase in pipeline bore are indicated, but be sure to consider how this will influence other parts of the system.

Reducing air flow Rate

Improved performance can often be achieved by reducing the quantity of conveying air, particularly if the system is over-rated for volumetric air supply. This could be achieved with a tee and a valve in the conveying air pipework (Fig. 3). In a positive-pressure system, these would be positioned between the air mover and the product feed. In a negative-pressure system, they would be placed between the filtration unit and the air mover. The tee and valve would also allow you to monitor the impact of reduced air flow rate on system performance.

Review routing

Review the pipeline routing and see if the number of bends might be reduced. Blind tees or sharp elbows should be exchanged for short-radius bends. For high-pressure systems with a single-bore pipeline, stepping the pipeline to a larger bore part way along, could also increase throughput.

Remember the potential role that pneumatic equipment wear can play on system performance, particularly when abrasive feeds are involved, and also consider the fact that hygroscopic products can build up within pipe walls. Be proactive, and check on any changes in system performance to avoid problems later on.

Wednesday, April 14, 2010

See Your Way to Problem-Free Air Conveying Systems

This is Part I of a multipart article that explores the causes of pneumatic conveying system performance problems. Part I reviews system throughput troublespots. Future installments will focus on the potential problems resulting from product and system differences, and the components themselves.

Pneumatic conveying is essentially a very simple process, but the design factors that influence system performance are varied and complex. Most component specifications are based on data resulting from pipeline design. Since the data used in pipeline design are not totally reliable, many systems incorporate margins and factors to allow for uncertainties. Use of these "fudge factors" often leads to a mismatch between components and over-design in certain areas. Although over-design will generally ensure that a system will work, it will rarely work efficiently.

Since the reasons for an underperforming system are not always obvious, we need to examine the likely causes of throughput difficulties, which result in frequent blockages, inability to convey a given product, and systems that fail to meet required duty.

Clogged arteries

One of the most serious and frustrating problems in system operation is pipeline blockage. To rule out blockage, check the obvious features:

Is the reception point clear?

Are the diverter valves operating satisfactorily?

Is the full conveying air supply available?

Was the pipeline clear on start-up?

If the pipeline blocks during commissioning trials with the pneumatic conveying system, either there is a serious system design fault or some simple adjustment needs to be made.

If system design is suspect, it is most likely because the air mover was sized incorrectly. A minimum conveying air velocity must be maintained at the product pick-up point at the start of the conveying line. The velocity depends on the product being conveyed and, for products that can conveyed in dense phase, varies with the phase density at which the product is conveyed. Since air is compressible, it is important to account for air pressure at the product pick-up point when evaluating the free air requirements for the air mover specification.

Air velocity at the start of the conveying line is particularly important. If this velocity is too low, the pipeline is likely to block. For products conveyed in dilute phase, or suspension flow, a 12-15 m/sec minimum velocity is needed. If a pipeline becomes blocked and the conveying line inlet air velocity is too low, then an air mover with a higher volumetric flow rate will be required.

It is important not to over-rate any replacement -- the conveying line inlet air velocity need not exceed the minimum conveying air velocity value by more than about 20 percent.

Overfeeding vs. incorrect air mover specification

The pressure gradient in the conveying line depends primarily on the concentration of product in the pipeline. If too much product is fed into the conveying line, the pressure requirement will exceed available and the line will block.

Each type of pipeline-feeding device has its own characteristic means of controlling product flow. In some cases, this is achieved by direct speed control, as with rotary valves and screws. With others, additional flow-control devices such as venturi feeders will be required. Control of blow tanks and suction nozzles is achieved by air supply proportioning.

Feed control is particularly important when a rotary valve feeds the pipeline, because a change of even one or two rev/min can have a significant effect on product flow rate.

It can be difficult to determine whether blockage results from an incorrect air-mover specification or over-feeding of the pipeline. For a positive-pressure system, this question can easily be answered by placing a pressure gauge in the air supply line at a point just before the product feed into the conveying line. In a negative-pressure system, the pressure gauge would be in the pipeline between the filtration unit and the inlet to the exhauster. Both cases will give a close approximation to the conveying line pressure drop.

Irregular feedrates

If the pipeline blocks only occasionally, this may be due to surges in product feed. In addition to determining the mean flow rate on startup, the regularity of the flow rate over short periods of time should be assessed. Differential pressure switches should be placed at all air movers and linked to the product feeder, to stop the feed in an over-pressure pneumatic air condition. This setup will give the system a chance to clear and can be arranged to bring the feed back online automatically. If a pipeline tends to block when the system is started up after a shutdown, some transient situation may be responsible.

Pneumatic Equipments That Costs Less

When it comes to power tools, pneumatic equipments are the ones that you can think of. These are tools that make use of air as the source of power. Some of these tools use air compressor in operations, while some use CO2 or carbon dioxide, which are usually stored in a small cylinder, for convenient portability.

These tools are commonly used in different industrial operations, especially for applications where electric or other motors are not applicable due to safety and protections. These tools are required and essential in all construction and manufacturing operations. For whatever kind of Do-It-Yourself operations you have, you will surely find a pneumatic tool that you can use.

Pneumatic tools are now being in demand, especially to industrial operators and construction workers. They prefer to use pneumatic tools instead of electric or battery-powered equipments because these tools are easy to use, more accurate, light-weight, less expensive, durable, and provide more power and torque when in use. Use of these equipments does not require the help of professional operators because these are usually user-friendly and easy to operate.

Pneumatic equipments are usually used in moving heavy loads from one location to another, especially in areas and situations where forklifts and cranes are not possible to be used. With the help of these pneumatic equipment and tools, your tasks and your operations will turn out successful and a lot easier. Maintenance is only in a minimum requirement since these kinds of tools rarely experience overheating because air is always present to cool them down. There are just some considerations when using these equipments. The tools should properly match the air compressor for better results and lesser occurrences of damages. The air hose should also fit the tools and the compressor. And the air pressure should be correctly adjusted according to the tools.

Purchasing pneumatic tools that you need for construction or just for any DIY purposes, you can find great deals from suppliers as the competition in sales and marketing for these tools are really growing. However, you would not definitely want to get just anything that is there. You would surely look for the best pneumatic equipments at affordable prices there could be. Finding the right pneumatic tools that have the quality and durability will ensure that what you paid for the equipments are really worthwhile.

Before you buy, search for the right supplier who does not only provide quality equipments but also gives importance to complete customer services for customers’ satisfaction. Some of them also provide training or initial guide for first time users and delivery and other after-sales services needed.

Repairs and maintenance may also be provided by the supplier. But to ensure you get all these services at low expenses but high on satisfaction, choose the right supplier. The company should have such skilled and knowledgeable manpower to be able to handle all the necessary and proper services you might need regarding the supply of the right kinds of pneumatic tools, including the services for repair and maintenance in case your equipments malfunction.

Monday, April 12, 2010

Solenoid Valve Selection: Don't Be Fooled by Flow Rate

Solenoid valve are widely used throughout the chemical processing industries. However, selecting the best valve for a given application can be difficult. Flow rate, a critical parameter for selection, can be calculated using various approaches. However, many of these methods are imprecise or yield non-dimensional results.

Complicating the situation is the fact that there is no single industry-accepted method for calculating gas flow rates for solenoid valves. Some valve manufacturers experiment with multiple formulas to determine which one will result in the most favorable- looking values for their valves. This practice can confuse end users, wasting time and money and compromising safety and efficiency when the wrong valve is specified.

This article summarizes the key issues involved in selecting solenoid valves for chemical processing applications, and discusses their flow properties and the methods most often used to calculate gas flow rate. In addition, it recommends a two-coefficient formula developed by ISA (Instrumentation, Systems and Automation Society), and shows how to use it to determine the best solenoid valve.

Solenoid valves 101

Solenoid valves use electricity to open and close an orifice in the valve body, allowing or preventing the flow of a given medium. In its simplest form, this type of valve is opened and closed by a plunger that is raised and lowered by the energizing and de-energizing of a solenoid. The magnetic field created by the solenoid's coil turns the plunger's stop into an electromagnet, attracting and raising the steel plunger. A corresponding spring compresses as the orifice opens. Upon de-energizing, the magnetic field is discontinued and the spring returns, forcing the plunger back onto the orifice and shutting off flow.

It is important to point out that in chemical processing applications, solenoid valves typically do not handle the medium directly. In many cases, the valve acts as a safety shutoff device for a larger system. Performance in this capacity is critical. A valve might be in the system but unused for long periods of time, even up to a year. When it is called upon to shut down the system, it must act immediately and predictably.

Solenoid valves can also be used to control or actuate other processes. For example, they can control the movement of other control devices such as large process valves that manage the application's media, or energize components such as desiccant dryers or venting systems, which require air pressure.

Let's review the basics. Flow rate is the quantity of a medium that passes at a given point during a given period of time. It is measured using the term CV, which represents the quantity of water in gallons per minute that will pass through a valve with a 1 psi (pounds per square inch) pressure drop across it. This measure is used to determine a valve's capacity at higher pressure drops, but also applies to both liquid and gas flows at pressure drops small enough that density changes are negligible.

Another, more accurate term for gas flow is "compressible fluid flow." Compressibility refers to a gas' ability to change density with temperature and pressure changes. Flow rates for compressible fluids are significantly more difficult to calculate than those of incompressible fluids, simply because of their properties.

The density of a compressible fluid flow fluctuates a great deal at higher temperatures and, especially, pressures. At lower pressures, the behavior of water, steam or inert gases may be very similar, but it changes wildly for gases when extrapolated to high pressure drops.

In cases in which a flow becomes compressible within the valve, effects might include cavitation, flashing or Mach number effects, making consistency in calculations even more difficult.

Flow path within the valve also can change the CV value (see Fig. 1). A straighter, more direct path means that the medium will have fewer fluid stresses applied to it as it passes through the valve. A tortuous (or convoluted) path will have the opposite effect. In fact, two solenoid valves that are the same in every way except internal construction and flow path can have completely different CV ratings.

Mounting and orientation of the valve, and corresponding gravitational effects, might also affect flow rates for certain solenoid valve types at very low pressure drop conditions.

With all of these potential issues, calculating compressible fluid flow rates for solenoid valves can be tricky. Compounding the confusion is the fact that there are multiple methods by which calculations can be made.

Calculation methods

Today, a few methods can be used to calculate compressible fluid flow rate values for solenoid valves:

Downstream pressure: This method is used by the National Fire Protection Association for pneumatic directional control valves. This equation approximates flow through an ideal nozzle. In the valve industry, it often is used to calculate CV for pneumatic directional control valves. However, it can overestimate the choked flow,"the point where decreases in valve outlet pressure cannot cause flow to increase, as commonly seen in ball, butterfly and solenoid valves.

Average pressure: The mean density equation is derived directly from equations for fluid flow through valves, and, because of its simplicity, is widely used in industry. However, because of the differences between gas and fluid (compressible and incompressible) flows, this equation can significantly overestimate flow for most valve styles, especially at high pressure drops.

Upstream pressure: This equation, like the others, is derived from an equation used for liquid flow. It, therefore, cannot be relied upon to work with choked flow situations. Again, it will overestimate flow for most valve types, especially at high pressure drops, and fail to predict choking.

So, what's the problem?

These equations are all used extensively by respected organizations and industrial governing bodies. There is nothing inherently wrong about any of them. However, dealing with the specific circumstances of compressible fluid flows and solenoid valves, these equations can provide only a non-dimensional view of flow rate.

So, why isn't there a single standard? Solenoid valves are used across a large variety of industries, whose end users are concerned about vastly different things.

However, it is clear that derivations of standard equations for incompressible fluid flow cannot reliably be applied to compressible fluid flows. The unpredictable nature of gases and their density changes means these equations can give inaccurate CV values at high pressure drops. Using these equations where they are best suited, at low pressure drops, gives a more precise, if one-dimensional, view of the valve's capabilities, not ideal for a prospective buyer.

There are other considerations as well. For customers in the chemical processing industries, the CV measurement is typically a benchmark for solenoid valve purchasing. Often, customers familiar with their applications know an approximate CV value needed for a new valve. However, they might be relying on an inaccurate number calculated using any one of the previously discussed methods. A manufacturer should, in this case, work backward with the customer and ask how this estimated CV was determined. If this is the case, the application usually needs to be analyzed again to determine the proper CV so that the manufacturer can apply the correct model valve.

Testing to verify flow rate is always a good idea, especially in chemical processing applications. When a solenoid valve is being used for actuation, the wrong CV can result in vibration or other anomalies in the system. In other cases, a valve may actuate a larger valve irregularly, causing the larger process or control valve to drop too quickly, slowly or forcefully.

Finally, consider the issues that arise for a potential end user trying to choose a new solenoid valve. These equations' non-dimensional views of valves' capabilities can result in incorrect information. Manufacturers can test a valve at a given pressure drop to determine the flow rate at a variety of data points, then plug these into any one of the above-mentioned empirical equations of their choosing to determine a coefficient. This coefficient may not describe the valve in a multi-dimensional way. Take the same valve and calculate different coefficients using the different methods and you could get different, less flattering CV values. A lot of calculations are averaged. It even is possible to rerun tests and calculations until the most favorable numbers are gleaned. Figure 2 demonstrates how even valves with the same nominal CV values might actually prove to have very different flow rates. The valves were made by different manufacturers, noted in the graphs by MFR X and MFR Y.

In an ideal world, customers and manufacturers would know that the same flow rate measures are being used everywhere. Until that becomes a reality, ISA's two-coefficient equation can replace guesswork with certainty, providing a multi-dimensional view of a solenoid valve's compressible flow rate at a wide range of pressure drops.

Friday, April 9, 2010

Stainless Steel Solenoid Valve Available In New Size

Magnatrol now offers its popular stainless steel 2-way solenoid valve in a 3-inch size. Valves are full port, and are said to require no differential pressure to open and are easily serviced while in the pipeline.

Applications include de-ionized water, ammonias, vegetable oil, fuel oil, gas, steam, solvents, cryogenics and oxygen. The valves are of a packless construction with continuous duty coils for all AC and DC voltages, available normally open or normally closed with 150- and 300-pound flanged connections.

Omega's SV-1200 miniature solenoid valves are suitable for applications in analysis technology, reliably handling difficult liquids such as acids, bases, pharmaceutical elements, and fluids in biotechnology processes.

Thermal isolation of the actuator and fluid ensures accurate measurements for metering applications. A perfluorelastomer separation diaphragm hermetically isolates the fluid medium from the actuator. Other features include universal functions, small size, and simple and fast electrical connection to reduce installation costs. An LED also provides safe and convenient monitoring.

Process Control Solenoid Valves For Water, Oil, Air, Gas, Steam, Cryogenics, Vacuum, Solvents, Brine, Oxygen, Corrosive Fluids

Every valve is manufactured and tested in-house following Quality Assurance Standards where production operations are under the control of our dedicated, experienced staff and workforce.

Many conveying lines consist of a single vertical upward line followed by a single horizontal line. If the horizontal line has an appreciable length, a velocity equal to or higher than the saltation velocity is required to maintain dilute-phase flow in the line. A significant reduction in the velocity required to maintain dilute-phase flow can be achieved if the horizontal line is angled downward as in Figure 1. A downward angle of only 15 degrees is enough to significantly reduce the velocity required to prevent solids salting out in the line.

Because it is more difficult to maintain solids in a dilute-phase mode in a horizontal line than in a vertical line, the saltation velocity is greater than the choking velocity. The ratio of the saltation velocity to the choking velocity ranges from approximately 3 to 6. This means that the minimum system velocity in a system composed of horizontal and vertical conveying lines in the saltation velocity. Many people try to decrease the diameter of the horizontal lines to simultaneously increase the gas velocity and to minimize the volumetric gas requirements of the system. However, decreasing the diameter of the horizontal lines also increases the solids mass flux in the lines, which means that the saltation velocity increases as well which generally results in no net “gain” by decreasing the line diameter.

Many solid pneumatic conveying applications have a requirement that the solids have to be conveyed in the dilute phase mode. In many of these applications, the conveying system consists of both vertical and horizontal pneumatic lines. The minimum velocity required to maintain solids in the dilute-phase mode in a vertical conveying line is called the choking velocity (Uch). The minimum velocity required to maintain solids in the dilute-phase mode in a horizontal conveying line is called the saltation velocity (Usalt).

Wednesday, April 7, 2010

Process engineering: Pneumatic Conveying Moves Ahead

Pneumatic conveying has long been a popular choice for moving bulk materials, either from storage facilities to a process unit, or between process units. However, pneumatic conveying technology itself hasn’t been standing still, and this can influence the choice between pneumatic and mechanical systems (such as conveyor belts or vibratory systems) and then among several types of pneumatic systems: dilute-phase, dense-phase or vacuum.

“Generally speaking, mechanical systems make sense with short, straight runs within a plant; they require less horsepower and sometimes can be a less expensive capital cost,” says Paul Solt, owner of Pneumatic Conveying Consulting, Allentown, Pa. “But they are usually a higher-maintenance choice, have problems with dust generation or contamination of process material, and are not as flexible in dealing with plant-floor configurations. Given sufficient capital, there is nothing that cannot be pneumatically conveyed,” he says.

Greg Steele, executive vice president for Dynamic Air, St. Paul, Minn., says, “Over the past 15-20 years, we’ve received a tremendous boost from EPA and OSHA. One by one, industries or applications where mechanical conveying has been the traditional choice have gone to pneumatic conveying. A decade or so ago, it was dry laundry detergent, then it was rubber processing and more recently pharmaceuticals. With pneumatic conveying, you reduce emissions and cut down on plant housekeeping requirements.”

Moreover, many new materials are more demanding to handle because of, for instance, reactivity or fire and health hazards; this also tips the scales toward pneumatic systems.

Because pneumatic systems run cleaner than mechanical ones and are less susceptible to product contamination, recycling materials is easier. A pneumatic system’s generally smaller product holdup also is an advantage for recycling. Some conveying systems are designed to handle different ingredients of a batch at different times, or must move the complete content of each batch together (which makes recycling of residues problematic). Mike Salvador, operations manager at Nu-Con Equipment, Chanhassen, Minn., says modern pneumatic systems need to be engineered with precise tolerances and should be capable of being disassembled, inspected and cleaned easily.

Entering another phase

No strict physical distinction marks the two main design options for pneumatic conveying: dilute-phase and dense-phase operation (vacuum conveying, which will be discussed later, can operate in either regime). Dilute-phase conveying is simply lifting and blowing powders or particles down a line, usually at higher gas velocities. Dense-phase conveying involves calibrating the line pressure based on the physical characteristics of the process material, trying to achieve full fluidization of material in the line, but moving it at a lower velocity.

“Dense-phase conveying was originally designed to meet the problems associated with the handling of abrasive materials,” says Mike Weyandt, sales manager for Nol-Tec Systems Inc., Lino Lakes, Minn. With the higher velocities found in dilute-phase conveying, particles can essentially sandblast holes into the elbows or connections of pneumatic systems, or can be degraded by impact with the walls of the conveying lines. “Many applications are now being handled with dense-phase systems because of process requirements that limit the amount of product degradation or separation allowable,” he says.


With dense-phase conveying, the designer strives to load the line with as much process material as possible and to run it at the most energy-efficient condition, which is just below the rate that would cause plugging. Over long distances or with high loadings, pressure variations can cause plugging and, to counter this, equipment vendors have developed various types of boosters that inject additional air as needed.

Dynamic Air, which has been offering booster technology for several years, is now introducing the DC-5 Air Saver unit . “Older boosters were simply put in place every 5 ft. or 10 ft. along a line and supplied a steady pressure,” Steele says. Some designers also experimented with adding pressure sensors and process controls to the boosters. “The DC-5 has a pressure-balancing valve that can regulate where pressure is applied automatically. In effect, the conveying line is constantly plugging and unplugging, which is the most efficient mode of operation.”

Meanwhile, Nol-Tec recently introduced its Air-Mizer injector, which is also designed to operate automatically to control conveying velocity in the line.

“The effectiveness of the dense-phase strategy is not guaranteed,” cautions Don McGlinchey, director of the Centre for Industrial Bulk Solids Handling at Glasgow Caledonian University in Scotland. “Much depends on the detail of the stressing mechanisms occurring during transport and the material’s response. A dilute-phase system can be fairly forgiving to changes in material specification, but these tend to be more critical in dense-phase systems, leading to many operating problems.”

Pulling a vacuum

Technically, the only difference between a pressurized system and a vacuum system is that the former pushes material through a line whereas the latter pulls it. However, the two systems pose distinct requirements for inlet feeding and outlet dispensing, and the physical properties of the material being conveyed or the process layout might make a difference.

“A vacuum system tends to make the most sense when it is dispensing to a single destination,” says Pneumatic Conveying’s Solt. If there are several delivery points, the designer can split the flow of a pressurized system with diverter valves, which is not as feasible with a vacuum system, he adds.

“Vacuum systems are limited in capacity by the difference between atmospheric and vacuum pressures,” says Herman Purutyan, a vice president at Jenicke & Johanson, a materials-handling consulting company in Westford, Mass. “With a pressurized system, you have the design flexibility to raise the pressure as high as you need.”

There’s certainly no vacuum in terms of suppliers. For instance, IEDCO, Sewell, N.J., is now offering modular technology from Volkmann Vakuum Technik, Soest, Germany, to the North American market. IEDCO representatives say the technology is particularly suited to high-purity applications, such as pharmaceuticals or batch mixtures where there is concern about material left from a previous batch. A user can obtain dilute or dense-phase conveying by selecting from among 60 different vacuum generators; tangential or radial suction ports accommodate material properties such as dryness or stickiness, respectively, to control flow characteristics. Discharge valves have their pneumatic components outside the conveyor body, allowing for easy cleaning in place, according to IEDCO.

Cyclonaire Corp., York, Neb., addresses the pressure question both ways. Its HC Series system, thanks to a venturi tied to a blower, can use vacuum in one part and pressurized flow in another. A typical application would be vacuum unloading of, say, a railcar into a transfer vessel, according to the company. When the vessel fills, the system automatically cycles to a discharge mode, using the same blower to convey material along to its destination. Optional load cells allow the system to weigh and batch the process flow.

Because the pressurized side of the system uses relatively low air pressures, the system is well suited to handling abrasive materials. At cement-maker R-Con’s Plant No. 6 in Wichita, Kan., the HC system unloads railcars carrying cement into the plant, where more than 200 concrete blends are produced in different colors or compositions to handle architectural requirements. The system addressed one pressing problem — the buildup of dust in an unloading pit that had been caused by spillage from a screw-pump conveyor — while raising capacity and productivity at the plant. “Our railcars hold 80 to 84 tons each, and we unload them in about two hours,” says Rick Heise, production manager. “There’s no need to get down into the pit, no dust, nothing to clean up. When you time everything out, we’re getting the job done much faster.”

Coming down the pipe

Most experts in pneumatic conveying agree that technology changes in the field have been evolutionary rather than revolutionary. Nol-Tec’s Weyandt says the company has introduced new broken-bag detectors and rotary feeders, which help streamline operation at the feed end of a conveying system. Pelletron, Lancaster, Pa., now offers several types of engineered elbows to improve the abrasion resistance of a conveying line. Nu-Con has launched a compact rotary-valve tube selector that allows a conveying system to feed multiple lines or to converge multiple lines into one; the unit has inflatable seals on all ports to ensure airtight conveying.

System design might be poised for potentially significant changes, thanks to the emerging commercial use of a new software combination: the tying together of computational fluid dynamics (CFD) with so-called discrete element modeling (DEM).

CFD, which has been used in commercial applications in the chemical industry for more than a decade, models continuous fluid phases such as air flowing around a shape. “Our multiphase models have been used to solve particulate flow problems where the focus has been the effect of fluid mechanics, as opposed to particle dynamics,” says Ahmad Khadari, a business manager at Fluent Inc., Lebanon, N.H.

“Classical applications of this technology include cyclone separators, fluidized beds or classifiers.”

However, to analyze a system from the perspective of the particles a “discontinuous” phase — another approach is needed, hence DEM. It originated, says John Favier, president of DEM Solutions, Edinburgh, Scotland, in geomechanics, where it was used to analyze a problem like the load of a building atop a gravel bed. “We’ve been constrained by the availability of computational power,” he says. “In the past, we were able to analyze thousands of particles in one system at a time; currently we can process hundreds of thousands, and very soon we will be doing millions.”

At that level of detail, modeling the interparticle effects of something like a dense-phase flow or a complex geometry within a conveying-system component becomes feasible. This can eliminate previously necessary simplifications and potentially provide more accurate results.

DEM Solutions is advancing with several efforts to have DEM address materials-handling problems in the commercial arena. Favier says the company has a project with John Deere, Moline, Ill., to analyze the flow of grain particles in its harvesting equipment. It also formed an alliance this fall with Fluent to combine its program, called EDEM , with Fluent’s CFD software.

Industry experts are taking a wait-and-see attitude. “DEM, or CFD for that matter, aren’t really ‘there’ yet,” says Jenicke & Johanson’s Purutyan. “A pneumatic conveying system can be very complex to model and, so far, all the simplifying assumptions you have to make limit the software’s predictability.” Instead, he recommends trying the actual process material in a test system and using the results for design.

Friday, April 2, 2010

Solenoid Valve Under The Hood Is One Of The Hottest Trends In Automotive Design

As a true lover of all things mechanical, I find the automobile to be one of the most fascinating solenoid valve we humans have ever created. Now that the fallout from the auto industry crashing and burning has settled, you can begin to see the outline of the many good things which are yet to come.

There are forward thinking trends all over the auto industry, and one of the hottest new car trends which I see evolving substantially during 2010 and beyond revolves around what goes on under the hood of our cars and trucks.

There is a lot of fringe activity within the auto industry on all things electric, with new batteries being developed, and many different flavors of new hybrid electric cars being designed, and quite a few hybrids being sold. It would appear that we are on the brink of a serious power plant design revolution. The standard system under the hood of most cars and trucks is a simple internal (or infernal if you don't really love them) combustion engine. In light of the fierce competition to keep this older technology in place, and maintain it as a viable contender in future designs, automotive engineers have to work harder to squeeze every bit of energy out of the smallest engines ever. The task is only complicated in that it takes quite a lot of testing and design work to reinvent something this simple.

Lets face it, if the internal combustion engine is going to survive, then it is going to have to get in shape, and really start carrying its own weight. One truth is that these damn things are truly amazing, yet even after all the time they have been around, they are still an exceptionally inefficient machine. What the engineering world is now tasked with is to advance the basic technology of the modern gasoline engine, and propel it forward into the new millennium.

Manufacturers are going to be putting more of their engineering focus on the efficient use of fuels, and by focusing on squeezing the most out of smaller engines, the engineers are moving quickly towards corporate efficiency objectives, while still maintaining a reasonable level of performance. It appears to me that the auto engineers are finding that the simplest tricks might be the smartest way to achieve their efficiency goals. There are also federal emissions and efficiency mandates in place which the auto industry needs to keep ahead of, or there will be serious financial consequences for any manufacturer which falls short of these goals.

The primary trend which I have been watching and hearing about for quite a while now, has become all about which power plant is being put under the hood of our cars and trucks! For most new car models the newest trend is to design and build them with smaller more efficient engines, with a secondary objective of maintaining, or increasing the power output of these pneumatic engines. With the upcoming technical enhancements, many of these smaller engines will operate near the same output of their larger predecessors. Auto engineers are accomplishing these complex design objectives by incorporating better electronic controls for their engines, and also by adding inventive new ways to operate critical mechanical parts of these engines.

One example of the heavy investment into this type of new technology is with a little car company called Fiat, which was recently merged with Chrysler. Fiat has pioneered a very unique internal combustion engine air intake control system dubbed "Multiair," in which the intake and exhaust valves are controlled by a special solenoid valve system. This "electromechanical" system is one which varies the opening and duration of the intake and exhaust valves, and this gives the engine management systems more and finer control over the actual combustion process.

What this means to the consumer is that they now can adjust the engines efficiency and performance by simply adding a special solenoid valve with specific controls that adjust to your driving demands automatically. If you are aggressively mashing the throttle, then the valves will be opened wider and longer, giving the engine more fuel, therefore more power, and when idling, or at other times when low power is all you need, the solenoid will automatically adjust the valves for smooth yet ultra efficient engine operation.

Incorporating this control scheme into many of the newer engines means that Chrysler cars will now be on the road to recovery with respect to gaining better mileage and keeping similar performance that Chrysler customers have come to expect. Now if only they could do this amazing control thing on a 440 "Hemi" engine! or better yet, on my 1995 Jeep six cylinder engine. That is a retrofit that I would gladly install onto my older cars!

There are a handful of other upgrades which will accompany these newer engines, and one of the first places we will see rapid advancements in the next few years is in the transmissions and controls for them as well. Automotive engineers are working on ways to increase the efficiency of their transmissions, especially the automatics, since they are inherently inefficient. also the auto manufacturers are excited to add hot toys which will help squeeze maximum horsepower out of the engines by adding cool gadgets like turbochargers, which for example you could get on a tiny 4 cylinder engine in their PT Cruiser, this gave the car great fuel mileage in normal driving conditions, and yet some fairly impressive torque when you really needed it!

In summary the more important trends are not about which color pallet will be coming out at the car show this year, nor about which DVD TV system will be in the new minivans, but I believe that it will be more about efficiency and performance, and this will be achieved with new Pneumatic technology under the hood!