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A diverse range of flowmeters, along with the turndown factors, is available for various flow applications, such as regular flow control (steam, gas, utilities, etc), process flow rates, fiscal or custody-transfer metering, and others. Most of these applications will be unidirectional, but some will be bidirectional.
The measurement of unidirectional flow rate is possible with all types of flow technologies, but the bidirectional flow measurement capability is required to measure the flow rates within the same flow loop in opposite directions. This sometimes creates difficult situations, challenges, process interruptions and/or measurement inaccuracies that can significantly affect the production and profitability of the plant.
We will further discuss the selection of the appropriate metering for bidirectional situations and applications, limitations, advantages and disadvantages, maintenance and installation costs.
Bidirectional flow lines are not very common in refineries and petrochemical plants, but if they are needed, they are always difficult. For bidirectional flow, the piping scheme uses the same line to accomplish delivery and/or control functions for flows moving in opposite directions (forward or reverse flow), depending upon the process conditions and objectives.
Examples of bidirectional flow are
The selection process of bidirectional flow metering depends on application requirements, process demand, end-user accuracy requirements and physical design constraints of the flowmeter itself. Various flowmeters are available with bidirectional flow capabilities, such as DP transmitters with an orifice, the Venturi or wedge element, Coriolis, ultrasonic, vortex, pitot, turbine and magnetic flowmeters.
Instances where a bidirectional flow measurement is required include
For bidirectional flow measurement between two process units in a process plant, for example, when two steam units are linked to each other, at the time of deficiency of steam in one unit, the other unit will supply the required steam to the deficient unit and vice versa. If reverse and forward flow rates are identical in both directions, and precise accuracy is not required, then dual transmitters, one for each flow direction, are the best solution for measuring the steam flows in/out of the plant. Two DP transmitters with an orifice plate, along with temperature compensation, can be used for the bidirectional flow. In this case, a non-beveled, square-edge type orifice plate should be used, and the two edges of the orifice should comply with specifications for the upstream edge mentioned in the ISO 5167 standard. It's also necessary to make sure of the full "upstream" straight lengths on both sides of the flow instrument. This must be clearly communicated to the piping design team during design reviews and before construction begins.
With this combination, do not expect high accuracy and turndown. This combination will provide the lowest installed cost with acceptable accuracy, as it is easy to maintain and replace. Also, this dual transmitter combination option will be ideal in cases where the transmitter will experience reverse flow once every four or five years for a four- or five-day period.
A single DP flow transmitter coupled to a primary element option, such as the special orifice plate mentioned above, can also be adopted for cheap reverse-flow measurement. This arrangement will cut down the expense of installing another (second) DP transmitter, orifice plate, additional hardware, meter installation requirements and the complexity of signal switching.
The square root function is complicated by the one-transmitter option because reconfiguration of the transmitter signal (4-12 mA and 12-20 mA) requires added function blocks and, subsequently, corresponding function blocks or logic at the distributed control system (DCS) side.