Instrumentation Interview Questions
Questions Answers Views Company eMail

what is plc? breif explain

APL,

3 5040

what is ment by PID controllers? explain with example?

2 5450

what are turbo generators?

1 2684

what is pneumatic control system?

APL,

1 4475

what is gas metering system? gas chromatograph? and gas compressors?

HPCL,

1959

what is HVAC?

1 5205

what is DCS and SCADA?

APL,

2 5204

whats the reason for control valve not installed -90degree (down position)

1 4130

What is the exact differences between HART,FOUNDATION FIELDBUS,PROFIBUS?

Jubilant,

3001

what diffrence b/w plc s7200,300,400

IFFCO, Reliance,

1679

What is the working principle of Dozing valve used in cement industry?

1 5388

If range of 3-15 psi, a multiplying relay with a 1:2 ratio would give what output pressure for 6 psi input?

1 3539

What is difference between reset and initialization in industrial automation?

Marafiq,

1 3906

If you calibrate a pneumatic pressure transmitter, how many adjustments are normally necessary or mandatory?

1 3721

i want use pressure transmitter for flow ,how?

Gasco,

5 8426


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Un-Answered Questions { Instrumentation }

in which principle pressure tx,level tx ,flow tx,temp tx ,control valve works?

2688


What you mean by multi stage control vavles?

1375


Explain Gas Turbine startup and shutdown sequences

3808


what about your moleg in pogrees with company

1799


what is installation and commissioning of (fat & sat) of power plant dcs ? this question keeps in desirable conditions of one company .

4398






Why is the orifice tab provided?

700


What is the purpose of bypass valve across AS valve.

1652


line up procedure for dp type flow transmitter?

1333


What is wet leg condition and why is it used?

1543


What is Span Error

200


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 =

1440


what is compensation? temprature & pressure

1564


What is sensitivity in vibration probes..?

1028


please any body have most important data for study for saudi aramco test of instrument QC thanks email shahnaveedullah@gmail.com

1231


use of split range ? where it is used ? in which control loop it is used ?

1476