please send the hpcl (instrumentation) model placement
papers to my mail....
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Answer / venkatesh
Please send interview questions(instrumentation) to my mail id: venkateshkadimi@gmail.com if anyone of you have them....
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Answer / sridar
please me hpcl (instrumentation) interview questions to
sinvel2009@rediff.com
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Answer / siva kumar
please send me interview questions.My mail id
sivak.kumar18@gmail.com
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Answer / mak
Please send interview questions(instrumentation) to my mail id: makhan.maity@gmail.com
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Answer / aishy
please send me interview question(instrumentation) to my mail id aishy.007@gmail.com
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Answer / mahad83
Please send interview questions(instrumentation) to my mail id:
mahad8331@gmail.com
Thanks
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Answer / sankar
plz send me some mechanical engineering interview question
and answers , few question papers
Is This Answer Correct ? | 1 Yes | 5 No |
if my flow is 20000 m3/h than which range of DPT i have to use????
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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 =
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I am using Capacitive type level transmitter for measuring oil level in a closed tank (lub oil tank). The txs range is 1500mm, and they do hunt regularly (for about 45mm), can anybody tell what could be the reason??? or any other type level tx that could be used to avoid this?
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Can u tell me the principle of the tc,rtd,level switch,pressure switch ,transmitter(pr flow level temp.),vibration...plz