What type of pump is are commonly used in auxiliary boilers?

1938

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Explain the advantages and disadvantages of using plastic and timber fenders?

1197

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How many attributes are there in column annotation?

373

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Is python interpreted language?

862

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What is lattice energy?

1187

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How do generative models relate to deep learning?

92

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we can add the no. of increase in shares due to exercise of options,convertible debentures,warrants etc.Why diluted eps is calculated separately?

2057

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How do I get to the root directory?

1055

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Can we call virtual funciton in a constructor ?

2217

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How to test java applications?

1059

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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 =

1953

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What is global and local controller in web dynpro?

325

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What is CTR and how one can calculate it?

543

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Explain clr?

1050

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What does executenonquery () method return?

941

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