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<title><![CDATA[DISCRETE TIME CONTROL DESIGN IN CHEMICAL PROCESS:]]></title>
<subTitle><![CDATA[CASE STUDY CONTINUOUS STIRRED TANK REACTOR WITH FIRST ORDER ENDOTHERMIC REACTION]]></subTitle>
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<namePart>0431105501 - Marthen Luther Doko, Ir., M.T</namePart>
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<namePart>Cefi Luthfi Muttaqien /142014042</namePart>
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<namePart>Dira Rianing Yonesih /142014056</namePart>
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<dateIssued><![CDATA[2018]]></dateIssued>
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<note>Modeling simulation and control is important in chemical process industries and it cant be solved manually because it’s mathematical
difficulties to simulate and control the modeled system is using computer programms. Analisys by identifying the process model of the reactor of this analisys is done by several methods given on the purpose. Methods used including feedback loop findings, determining of stability and testing the responses using impuls and step input. The continuous response of the reactor is converted to discrete response by using time sampling. The analyzing the stability of the system used root locus, Nyquist plot and jurry analysis</note>
<subject authority=""><topic><![CDATA[Feedback;Stability;Response;Discrete time;]]></topic></subject>
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