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1.2. 5 Kae tee tn dto op amd 55 Summary ls ma ya sp par pea tasa ar Seat EU Ee um de toas t cl 56 Appendix 6 Distillation Controller Tuning 61 Introduction to the Virtual Process Control Lab VPCL Objective What Is MATLAB Dan maan omniom ma van sq nl iy nc ye re iy BTL oan i i ma iy m MATLAB ly of spe pce akan tes Stig at metas cone MATLAB fe S dut i ay 613 Simulink Sl ia page mil ig ad ming us miee ei nae Dal a Fot dg pda o a mdi RU rcc E yeah pve ae dq ie paro fce qut ay mace and ac eques and wen can Yar em wes kaqt ha elect acha I tie 614 Overview of PCL s LETS wa Visual Process Control Lab way 615 Ending Sesion 616 Summary Padi i lot cal Pa pl 63 First Order Plus Time Delay FOTD Transfer Function 634 Introduction pa aa a a wer pc ne tn be SST ES MAO was E MTS E a ACA po 632 Procedure Colum 1 haggis 2 meng etna hic ela o aga Angie et
3. m 17 Appendices 174 Appendix A s aw Chanseaf Process Qupa Tange e Prcen ec Process Model incisive Caral Ve oupa B T p i ang in ete ean Y meet UL Fa A Inogramig Process Reaction Curve po EE u gt Test E change in eate sin 1 Pig Deadsime Procesi Reaction 172 Appendix pem LN EU ran pm PPZ 200 mI er o dl 2 Modelling Heat Exchanger Pilot Plant 21 Modelling Heat Exchanger Pilot Plant eo M E st sce te 244 Objective Stat Opn Loap Core 22 Preparati Start Experiment 24 Open Loop Con
4. Objective sa anan e is ganas 83 Transfer Function Based Simulation experto em das ln pn Ya imaq naam sms IE ews i LI at IS a ara tune Te one tan KANTU wip er ea ecco eve nines owe mmc ane ws m ne p a ee Sa ts hu a en ge ee Ta ie gal See E ang Seni ti De Sa een ts aga i sph na in y e ago ika ek dae ep Te scam pen ine ot gy ad iur sap kare Vr a oa Acha sa in m s a ae Sr i Wirupa ree Ao con en Ac MIE mop E Si ae soci MAR ea ec Nace eem App se az ey en vine Mgt Sin nk camp th pgs ma ss Fague a se 3 Ta e paa aaaea swears San Mgt Tens een o lg pret Sm tant yom a as Ange cd ee HMULINK ay ag ey alto macs ali dci epiac Yes wah a L cn Uae wan imay hen Que ee ss o MATIAN r EEE tna hr te SIMUL eye ret Peep pal atoning ape tn Mer Pee ep pile oig Pee ep eile ing pe yu E SUMMARY 85 APPENDIX
5. Ting Rena Aah ee poer SS A a a Date mm manaa Cnr Teng stunt Se er Tine ay POTD Tr Tareh Programa Lagi Contar pom et Poo in ug Com ae me ion in tasta 1 Level Control Pilot Plant necem pu SEIS Cnt a ten AZ je 14 Simple PID Level Control LIC 221 CD600 Self Regulating pac sumi cap ce a el a sam ini enda ind wo ea oa ae ee of a Si pc yb i irt ibe P la hin pees ya Bor Bran Lave ce and ia sea ues ern ol it Sie th Pin Ag Paz d Sepa pc SET lO a pawanan ded Cat iii 144 Objective 142 Results 12 Prepara 13 Section Identification 144 Start Experiment 132 Results Analysis 14 Section B Open Loop Tuning Method 142 Tabulation and Analysis of Results on C Closed Loop Tuning Method 151 Start Experiment
6. te aqu Mae we ea J bs leo ha o y pi me he pen me pi op e pd Ben nn rer p 222 0 wam te Vapeur Fo Bate waseq and a She ig ta ge Yodo eo sg at mi CAUTION Chae alta name ar run era tran d t kema anta nganan oan inc fds dle eu Tee x te tfr Kas ch P gupta as vale pu sr ie an Kapan mn me cd one np nt aw Ga Aa Mens xi ape nf oes a pone ape PC pe daa E mame ti Ey mig me aid wen ae i Lak To eda ca e E a ge eh ae n has as an st by ie a De wa w te lot rk e uta rs Sa Ro Var ln va mar Var gn i puas ea Pa kram 0 Ta Or Cot t aie at ie tse keh an ana Mg e mas ng A is tt y ery ce nen Tce deg he i a ute peli nee a pen ere ceti te Mi t be bg rd eg the S tw te cane tae Qui pia of ds ug st ih ee o Id ap oe sd vig Pion a Pe tl aw
7. SKC 5771 Process Gontrol Laboratory Student s Manual Second Eton and Revised KAMARUDDIN ABD HAMID AHMAD KAMAL BADERON KHAIRIYAH MOHD YUSOF MIMI HARYANI HASSIM Proc Safety Group SKE 5771 Process Control Laboratory Student s Manual SKC 5771 Process Gontrol Laboratory Student s Manual Second Edition and Revised MOHD KAMARUDDIN ABD HAMID AHMAD KAMAL BADERON KHAIRIYAH MOHD YUSOF MIMI HARYANI HASSIM Process Control amp Safety Group Preface w Course Objectives PP so tas d a usss a ny was nenn pe pan ii es esper snes hn pen a ney UY de ae esp wc en tt voy L iat sl ea eddy p pei loa nd pesamuan aicut Lab Experiments wF Ht hno PAP PLC Groups Teams Er Teen jose rg cc cng Tote vs ha ce LS a aan anjaba ng rm open man am a Pepes Aa ner ea is pa st Safety pcs i ig de my Ss ag gt m Students Performance Evaluation epo Yot wil da sI Er Sy tre cid we diya un mh mu Set a mg of ee dig Oi roan ae No ae gts at ap u Yo ad Contents sagte CCD m uc She En Log
8. a te i maw a ot a he i nb Mai Pepe mc hay Vpn ee hte wg I pte cli rice ma sa nen Pa Ej i en een ac a a 64 Cohen Coon Tuning Method 64 1 Introduction ee s PA 5 M mh anty ane beline anging cbr e a ite ta Ie nima Ama wet Tane AOH Can oai ie mias he Dal Cata stage ac ee Cam wang me Den 65 Summa RET te ms pc lo po u in uni m tampe nc ate Ra Reip dd p doa 7 Programmable Logic Controller 73 Classes of PLC s 7A Elements and Description Coma Testa A u 75 Sensor and actuators sy 76 Uses of the PLC 7 Software Recall of digital electronics a wana ha web be Auen 4 Be Puch oe nly mt SEAS lt iy yo sn erm i eh ey ps ta hn B pn tes pc dingo e PL AS De acan e maca wea pe st epee pe Wie api hth ne li ae ample Bo Gt eng c pp ant cael cal ae eric sat home eon mel po E 5 A 8 Dynamic Simulation in Simulink
9. ay 513 Simulink te pie moin sg ad ming us Spe ae in nae ne Del Wetan satun ne pt a il e apah sd gan ng tng eur met yc yh pvr sate yx Loma acid patas ioe saca wa pu pga Sa ls oi o Mona e can maki wing Ya em wes a Ben eek 544 Overview af PCL Ve Pcs Lab VE pogum ver enge in suing WAR AR aw eee uma S kasa wran Visual Process Control 515 Ending Sesion Tan dc us wa ton ae Nan New ake yoa a 516 Summary Vital Process Control Lab way 52 Objective 53 Introduction Procedure Furnaee 544 Proportional Control EEE ean Sep ug sup Ten wy K adipe De 542 Proportional Control for a Disturbance Mo ean atanp ie Omi rah sao akah se he pi sena e 543 Proportional Integral PD Control m actam sey um 0 Fem ate vee costing opus he pone on 44 Proportional Integral PD Control for a Disturbance ghey u hte qut esent adco Wae ten arga u HD Roo 18 19 long aa af de
10. lant us pom 3 Tel en saa me itas Each be is geneste i soe L p 43 Display pomum Atte See poe sa al Ve Eo va usa dat rd ono 44 Step By Step Operation tasca ere Wl bel py sepia he oi AAA startup SESTO SEREEN pem oe was MAIN Sie ne EA ug un ba 442 Flow Control Bye LEN CONTROL pd ae Tek Cg Ca og po lt san ag dee ne oe zin FLOW ad pos Cue ane M Qo Ya els mee anar w ONOFF ha st ee jn dea uta x S duae sam mee w AUTO MANUAL he am Nevo in adn ps Eas a rn a i pa ae pe at nas a na AME nr pV ae a a a Toca cal ae us haw lp saha pea s 5 Steady State Feedback Control Per 4 Introduction to the Virtual Process Control Lab VPCL 514 Objective What Is MATLAB m Das maan onion md ei sq th yc ye een iy BTL i fe i ms cp ae MATLAB of apa ci call tls Voy met cn MAAR Cent ony a op esd Sipe in AA ee ba a
11. ng 322 Results Analysis on B Control Loop Performance Test 331 Sturt Experiment 332 Tabulation and Results Analysis Appendices 341 Appendix A s D Chanseaf Process Qupa Tange e Prcen ec Process Model incisive Caral Ve oupa B T p i ang in ete ean Y meet che cop Integratnig Process Reaction Curve po HE u gt est E sn 1 Pig Deadsime Procesi Reaction 342 Appendix B pem Le pm PPZ 200 mI er o dl 4 Flow Control Pilot P
12. troller Tuning 244 Results Analysis 25 Appendices 251 Appendix A s D Chanseaf Process Qupa Tange e Prcen ec Process Model incisive Caral Ve oupa B T p i ang in ete ean Y meet UL Fa A Inogramig Process Reaction Curve po EE u gt Test E change in eate sin 1 Big Deadsime Procesi Reaction 252 Appendix pem LN EU ran pm PPZ 200 mI er o dl 3 Heat Exchanger Temperature Control Pilot Plant Exchanger Temperature Control TICI37 See ing e pul h o ois my ee iri Pan d Objective 312 Results 32 Section Closed Loop Starr Experiment Closed Loop Tuni
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