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 =
No Answer is Posted For this Question
Be the First to Post Answer
how to calibrate the temprature transmitter MURCREYtype and thermocouple input type.
What is the minmum distance between the electrical panel and Instrument panel
what is the imbustion control loop
i have steam drum height 1000mm. and i want to placed the transmitter below the tap.how i calculate.
wt is cold junction compensation
what is pico fuse? how this different rom othe fuses and how to locate it inside the card?
How to get Cv of control valve having following parameter ,i.e inlet pressure 4.5kg/cm2 outlet pressure 1 kg/cm2 specific gravity 0.808
for commissioning the DPT and Flow Transmitter , what kind of necessary activities we have to check and do? specially that orifice flange valve[ isolation valve}
Identification of ss fittings, pilot valves, relief valve.
generally for transmitter we are giving supply 24vlts?but we are getting output 4-20ma ? how it is possible? is there any operation inside the tx?pls give complete information?
how to use level tranasmitter in closed tank application.?
selection of the zener barrier for the hazardeous area zone 0
Civil Engineering (5086)
Mechanical Engineering (4456)
Electrical Engineering (16639)
Electronics Communications (3918)
Chemical Engineering (1095)
Aeronautical Engineering (239)
Bio Engineering (96)
Metallurgy (361)
Industrial Engineering (259)
Instrumentation (3014)
Automobile Engineering (332)
Mechatronics Engineering (97)
Marine Engineering (124)
Power Plant Engineering (172)
Textile Engineering (575)
Production Engineering (25)
Satellite Systems Engineering (106)
Engineering AllOther (1379)