how eddy current loss in probe and induced gap voltage accros probe trip and shaft
Hai friends I have dought for O2 analyser how to working in boiler area. And what is the basic principles
tell me the temp range of rtd?
How to calculate P,I&D value in PID controller ?
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what is working principle of presure and temperature guage?
the square root type transmitter r used to which applications
sir, give me placement papers and interview quistion of birla group company of copper.
how to rectify the problem ,if we erected the DPT instrument wrongly of hp on lp side and lp on hp side?
hi i want sov loop cheak from consol to field the operater given status to sov still no change, but MR room to sov ok so whats a problem and alreasy cheak all conection ok ?
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 =
How many types of sensors are used in instrumentation & what are names
what is your eligibility criteria for freashers?
If we increase only P what will be controller action ?
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