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Showing posts from November, 2015

Velocity Averaging Pitot Tubes for Air and Gas Flow Measurement

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When it comes to measuring the flow rate of air or gas in a duct, there are many different devices used.  For example, there are thermal sensors, hot wire anemometers, rotating vane anemometers, static pressure drop devices (venturi, orifice plate), and differential pressure devices (pitot, annubar, primary element).  The most widely used and considered a true measurement of the flow is the differential pressure device.  The most widely used differential pressure device is a velocity averaging pitot tube. Velocity Averaging Pitot Tube The velocity averaging pitot tube is a device that when inserted into the air or gas flow stream, provides a high pressure measurement port and a low pressure measurement port.  The high pressure port measures the total pressure created when the air or gas stream impacts the port, where the low pressure port typically measure the static pressure in the duct. VAP³ Velocity Averaging Pitot Tube from Eastern Instruments The difference between the

How to Fix your Weigh Belt Feeder without major changes to your process

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Weigh Belt Feeders have been widely used for many years to measure the flow rate and totalization of solid materials in a process while providing a feed device to move materials through that process.  For some products they can be accurate enough to keep in your process and deal with their calibration issues, but for some products, they can be a maintenance nightmare and something that needs to be replaced.  However, with their large footprint and complex installation, finding a replacement feeder that fits can be a real issue. One way to deal with this maintenance issue but to still have that vital process measurement is to install a flow meter that can be installed at the end of a belt conveyor.  Since the Weigh Belt is in essence a belt conveyor, it would be used as just a material handling device and not a flow meter.  Once such a device that can fit in such a tight space is the CentriFlow Type I meter from Eastern Instruments. CentriFlow Type I Meter The Type I meter

Controlling the Flow of a Solid using a Feeder with Integral PID Control Capabilities

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Measuring the Mass Flow Rate of a Solid Material can be hard enough, but when a process needs a Controlled Flow Rate as well, this can be really difficult.  Controlling the Flow Rate in a process requires a PID control loop, where the input is an accurately measured flow rate and the controlling device is able to provide a fast change when an input change is noted, without overshoot or undershoot. In most industrial plants, these types of flow controls are typically done by a PLC.  These same PLC's usually take in all of the inputs of the process and compute all of the outputs to all of the devices in the process.  The loads on these PLC's can vary greatly and typically result in a long scan times that can adversely affect the PLC's ability to provide the best PID control loop.  This makes the control of the loop inaccurate, slow, and creates difficulty when trying to tune the loop to obtain the highest degree of control. The best way to get around these issues is to us

Air Flow Measurement Accuracy within a Particulate Laden Air Stream

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Measuring the Air Flow in a duct can be difficult enough when the flow profile is not free from turbulence, disturbances, cyclonic flow, and reverse flow, but add to that particulate, ash, dust, or debris in the air, and it can almost be impossible.  So, how do you get accuracy when trying to measure the Air Flow in a duct that has particulate, ash, dust, or debris in the air stream? The traditional way is to use a blast purge or blow back system that will take high pressure compressed air and blow it back through the high and low ports of the air flow pitot or flow element so that any particles, ash, dust, or debris is blown out of the ports on the probe.  This not only uses a lot of compressed air, which needs to be completely dry to work properly, but it also requires a complex system of valves in order for this to be done automatically.  If the blast purge or blow back is not done on a regular basis, and if the particulate, ash, dust, or debris level is high enough in the duct, t