where can i learn VB scripint ?

2105

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How to replace perl array elements?

953

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How do I zip a powerpoint on a mac?

405

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Does every abap/4 have a modular structure? : abap modularization

1133

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How do I find information about the install locations for the various instances running on a computer?

1086

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What is transpose?

120

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What are the type of flags to run an application in android?

1109

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How do I rename a procedure?

886

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Can a standard object become child in master detail relationship? : salesforce objects & fields

492

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What is hibernate used for?

472

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What is c++ course?

1058

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why the word trasfection is prefers for transfer of genetic material through non viral particles ineukaryote not for prokaryote?

1161

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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 =

1950

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Differentiate between hdam and the hidam databases?

1050

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What is modeling?

1063

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