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<title><![CDATA[DISCRETE STATE ESTIMATION DESIGN IN CHEMICAL PROCESS CONTROL CONTINUOUS STIRRED TANK REACTOR]]></title>
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<namePart>0431105501 - Marthen Luther Doko, Ir., M.T</namePart>
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<namePart>Veni Annisa Marley /142014012</namePart>
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<namePart>Iqbal Rizaldi Maulana /142014035</namePart>
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<place><placeTerm type="text"><![CDATA[Teknik Kimia]]></placeTerm></place>
<publisher><![CDATA[FTI]]></publisher>
<dateIssued><![CDATA[2018]]></dateIssued>
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<note>Modeling and simulation is done to facilitate analysis on control system or control system designed based on continuous concept. A prcess system must be able to control, so that all of mathematic parameters can be calculated based on constrains imposed in the respon. The purpose of this research is to design a control and observer by using ackermann method. Which observers and controls to estimate the expenditure of the control system. The design of an adaptive observer is based on the combination of a state observer that could be used to estimate the state variables of aparticular plant state-space representation with an on-line estimation scheme. Begin with observable canonical form one can find observability matrix of n linear independent rows. The various canonical forms known also as Luenberger canonical form can be obtained. The Observer called Adaptive Luenberger Observer .</note>
<subject authority=""><topic><![CDATA[ackermann method, estimation]]></topic></subject>
<subject authority=""><topic><![CDATA[control andobserver, system identification]]></topic></subject>
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