Explain Split Range Control In Control Valve Briefly.
Answer Posted / www.islamqa.com
perfect answer sam as usual
and if there is something else to say I can say that split
range control ( or call valve sequencing ) is a technique
used for satisfy the procsee requirements.
Actually we have techniques and modes for this strategy.
The used techniques to achieve valve split
ranging /sequencing are:
1 - Valve bench set adjustment (modify the valve itself)
2 - Positioner adjustment
3 - I/P adjustment
4 - Using 1 controller with 1 I/P and 2 adjusted valves
and this is very slow process as we have to wait a long
time till the pressure is built up witin the loop.
5 - using 1 controller with 2 series I/P
and here we face the risk of voltage drop.
6 - using 1 controller with dual o/p.
7 - using 2 controller with the same input.
# And we have 3 main modes for this strategy:
1 - COMPLEMENTARY:
where 1 of 2 valves opening is opposite to the other
@ 4 ma valve-A is fully open while valve-B is fully closed
and thier stems move synchronously.
2 - EXCLUSSIVE
3 - PROGRESSIVE
Ahmed Sabry
Control and Instrumentation Engineer
GPC - General Petroleum Company
ahmedsabry.online@gmail.com
CELL.: 00 2 0121367310
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Q1: Consider part of a control loop, which excludes the transmitter, consisting of a process, a controller and a control valve which may be represented by two dead times of 0.5 min each and three exponential lags of 0.8 min., 1.0 min. and 1.5 min. respectively. We wish to express this system as an overall first order plus dead time (FOPLD) model ie gain, time constant and process dead time. (We will see later that this is often done, to simplify controller tuning). For this exercise, gain is considered to be 1.0. (A) If the transmitter is a flow transmitter whose behaviour can be described by a dead time of 0.2 min. and an exponential lag of 0.5 min. in terms of the overall dead time and overall first order lag how can the system behaviour be approximated ? Overall dead time = Overall time constant = (B) If the transmitter is a temperature transmitter with a temperature sensor in a protecting well whose behaviour can be described by a dead time of 0.7 min. and an exponential lag of 15 min. how can the overall system behaviour be approximated now? Overall dead time = Overall time constant =