Siemens PCS 7 manual Pressure Control in Tanks

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Introduction

feed water tanks. There are different objectives for level control according to the plant context [also see Related Literature /2./]:

Keep level constant (exactly at the set point) – important for levels directly in- fluencing the process; disturbances are passed through to the output (drain).

Keep level as small as possible – if “dead volume” and inventory are undesir- able.

Keep level inside specified limits while using the tank as buffer – changes in level are tolerated to achieve a smooth drain flow.

Figure 2-3 Examples of level control (marked in red) in a typical part of plant (distillation column) [also see Related Literature /1./].

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2.3.2Pressure Control in Tanks

In some cases the pressure control in tanks behaves in a similar way as the level control. The control loop shows an integral behaviour, if the manipulated variable is a gas feed (e.g. admission of inerts) and no pressure loss to the environment ex- ists. Typically a separate purge valve exists in such cases to discharge gases. The pressure controller uses a split range function to access either the feed valve or the purge valve.

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MPC Level

V 1.0, Beitrags-ID: 42200753

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Contents Applikationen & Tools Page Online-support.automation@siemens.com Warranty and Liability Table of Contents Preface Objective of the ApplicationBasic Principles of Model Predictive Control IntroductionStable and Unstable Control Loops Whithout compensation With Ohne Integral Ausgleich Examples of Unstable Control Loops Level ControlPressure Control in Tanks Position Control Stabilization of Unstable Control Loops Unit-step response of an integrating processt 1s PID Tuner Starting Point Configuration of MPC with Slave ControllerConnection in CFC MV1 MV2 Connection of MPC and slave controller Commissioning Simulation Example OS picture of the example project Conclusion Related Literature Internet Link SpecificationsBibliography History Version Date Modifications
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PCS 7 specifications

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