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Friday, November 30, 2012

The Variable Area Flowmeter

The variable-area flowmeter (Figure 1) is among the oldest technologies out there and arguably probably the most well -known. It's constructed of a tapered tube (usually plastic or glass) and a metal or glass float. The
The plastic or glass tube of the variable-area flowmeter lets the user visually inspect the float, whose position in the tapered tub is proportional to the volumetric flowrate.
volumetric flowrate by means of the tapered tube is proportional to the displacement of the float. 

Fluid shifting by means of the tube type bottom to top causes a pressure drop throughout the float, which produces an upward force that causes the float to move up the tube. As this occurs, the cross-sectional space between the tube partitions and the float (the annulus) will increase (therefore the term variable-area). As a result of the variable-area flow meter relies on gravity, it have to be installed vertically (with the flow tube perpendicular to the ground). Some variable-area meters overcome this slight inconvenience by spring loading the float within the tube (Figure 2). Such a design can simplify installation and add operator flexibility, particularly when the meter have to be put  in a good physical  area and a vertical installation will not be possible. 

This variable-area meter with a spring-loaded float can be installed at any angle. This accommodation is not available for traditional variable-area flowmeters, whose operation relies on gravity.
Two varieties of variable-area flow meters are usually available: direct-reading and correlated. The direct-reading meter allow  the user  to read the liquid or gas flowrate in engineering units (i.e., gal/min and L/min) printed directly on the tube, by aligning the top of the float with the tick mark on the flowtube. The benefit of a direct-reading flowmeter is that the flowrate is actually read straight off the flowtube. Correlated meters, however, have a unitless scale (sometimes tick marks from 0  to 65, or 0 to 150 ), and come with a separate data sheet that correlates the scale reading on the flowtube to the flowrate in a particular engineering unit. The correlation sheets often give 25 or so data factors alongside the dimensions of the flowtube, allowing the consumer to decide the precise flowrate in gal/min, L/min, or whatever engineering unit is needed.

The advantage of the correlated meter is that the identical flowmeter can be used for numerous gases and liquids (whose stream is represented by completely different units) by choosing the suitable correlation sheets, the place further direct-reading  meters would be required for different fluid applications. Equally, if strain or temperature parameters change for a given application, the person would simply use a special correlation sheet to reflect these new parameters. By comparability, for a direct-reading meter, a change in
operating parameters will compromise the meter's accuracy, forcing it to be returned to the factory for recalibration. Usually, the typical accuracy of a variable-area flowmeter is ±2-4% of fullscale flow.

Advantages: The main benefit of the variable-area flowmeter is its relative low cost and ease of installation. Due to its simplicity of design, the variable-area meter is virtually maintenance-free and, hence, tends to have a long working life.

Another advantage is its flexibility in dealing with a wide range of chemicals. As we speak, all-Teflon meters
can be found to resist corrosive injury by aggressive chemicals. The advantage of a Teflon flowmeter with a built-in valve is that you would be able to not only monitor the fluid flowrate, but you can control it, as well, by opening and shutting the valve. If the application requires an all-Teflon meter, chances are the fluid is fairly corrosive, and plenty of users would like the option of controlling the flowrate by merely turning a valve that is constructed into the flowmeter itself.

Disadvantages: One potential drawback of a variable-area flowmeter occurs when the fluid temperature and pressure deviate from the calibration temperature and pressure. As a result of temperature and strain variations will cause a gas  to increase and contract, thereby changing density and viscosity, the calibration of a specific variable-area flowmeter will now not be valid as these circumstances fluctuate. Manufacturers sometimes calibrate their gas flowmeters to a standard temperature and pressure (often 70°F with the flowmeter outlet open to the environment, i.e., with no back pressure). During operation, the flowmeter accuracy can rapidly degrade as soon as the temperatures and pressures start fluctuating from the standard calibration temperature and pressure. Meters used for water have a tendency to indicate much less variability, since water viscosity and density changes little  with normal temperature and pressure fluctuations. While there's a strategy to correlate the circulation from precise operating situations back to the calibration conditions, the conventional formulas used are very simplified, and don't bear in mind the impact of viscosity, which can cause large errors.


Thursday, November 29, 2012

Primary Definitions and Terminology used in the field of Process Control


As we'll observe two of the most important indicators used in process control are referred to as Process Variable or PV and the Manipulated Variable or MV. 


In industrial process management, the Process Variable or PV is measured by an instrument in the area and acts as an input to a pc based mostly automatic controller which takes action primarily based on the value of it. Alternatively the PV will be an input to computer primarily based hardware system and its value displayed in some method in order that the operator can perform manual control and supervision.


The variable to be manipulated, so as to have management over the PV, is called the Manipulated variable or MV. If we control a particular movement for occasion, we manipulate a valve to regulate the flow. Here, the valve position  known as the Manipulated Variable  and the measured move becomes the Process Variable.

Within the case of a easy automated controller, the Controller Output Signal (OP) drives the Manipulated Variable. In additional complicated computerized control techniques, a controller output signal could not all the time drive a Manipulated Variable within the field. In apply, the time period Manipulated Variable isn't
used. Most individuals involved in course of control seek advice from the output of a controller and it is assumed that one knows the purpose of it. The perfect worth of the PV is usually known as Target value. and within the case of an automated management, the term Set Point Value is preferred.

Varieties or Modes of Operation of Available Control Methods
There are 5 basic forms of management accessible in Course of Control. These are:
• On-Off
• Modulating
• Open Loop
• Feed Forward
• Closed loop

Probably the most primary control idea is ON-OFF Management as found in a contemporary iron in our households. This is a very crude type of control, which however ought to be considered as an inexpensive and effective means of control if a reasonably large fluctuation of the PV (Process of Variable) is acceptable.
The damage and tear of the controlling component (solenoid valve and so on) wants particular consideration. Because the bandwidth of fluctuation of a PV is increased, the frequency of switching (and thus put on and tear) of the controlling element decreases.

Modulating Control

If the output of a controller can transfer via a variety of values, we've got modulating control. It is understood that modulating control takes place inside an outlined operating range (with an higher and lower limit) only.
Modulating control can be utilized in each open and closed loop control systems.

Open Loop Control

We have now open loop control, if the control motion (Controller Output Signal output) is just not a perform of the PV (Process  of Variable) or load changes. The open loop control does not self-correct, when these PV’s drift.

Feed Forward Control

Fairly often it is a form of control based on measured disturbances (Feed Forward Control). It's a type of Open Loop control as the PV is not utilized in the control action. Feed forward is a more direct form of control than discovering the correct value of the manipulated variable (MV) by trial and error as occurs in feedback control. In feed forward the foremost process variables are fed right into a model to calculate the Manipulated Variable (MV) required to manage at the Set Point (SP).

The proper industrial use of this sort of control is, for instance, to incorporate this with suggestions; or closed loop control. Then the imperfect feed forward control can correct as much as 90% of the upsets, leaving the feedback  system to appropriate the 10% bias left by the feed forward component.

Closed Loop or Feedback Control

We have now a Closed Loop Control System if the PV, the target of control, is
used to find out the control action.The idea of Closed Loop Control is to measure the PV (Process Variable); examine this with the SP (Setpoint), which is the desired or target value ; and decide a control motion which ends up in a change of the Output value of an automated controller. Most often, the Error (ERR) time period is used to calculate the OP value. ERR = PV - SP. If ERR = SP -PV has to be used, the controller needs to be set for REVERSE control action.