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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 =
axial displacements of the turbine. What could be the causes?♪ ♪
Hi all, I am using windows vista, I am in the process of learning QTP. When ever I try to work with insert mode in flight application , i am getting the error of 'Operation must use an update table query, fractional truncation(null) error. Can anyone help me regarding this?
i want to know how can i divide the bandwidth among two computers.say i have a connection of 256 kbps dsl connection. i have a switch.now i want to divide this 256 kbps in two 128,128 equal connections.so that both of us can work on our separate 128 speed
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Calculate the molar extinction coefficient of a solution containing 5 *10-4 g litre-1 of a biomolecule, molecular weight 275 g mol-1, and absorbance 0.75 in a 1.2 cm cuvette.