000 01970naa2a2200325 4500
001 570936
005 20231030032025.0
035 _a(RuTPU)RU\TPU\prd\268682
035 _aRU\TPU\prd\268681
090 _a570936
100 _a20170111a2016 k y0rusy50 ba
101 0 _aeng
102 _aRU
135 _adrcn ---uucaa
200 1 _aComparison of non-linear, linearized 2nd order and reduced to FOPDT models of CSTR using different tuning methods
_bElectronic resource
_fMunna Kumar, R. S. Singh
203 _aText
_celectronic
300 _aTitle screen
320 _a[References: p. S75 (17 tit.)]
330 _aProcess modelling and design of controller based on the process model is an important step in the process control. In the present study three different mathematical models i.e. non-linear process model, linearized 2nd order model and first order with dead time (FOPDT) model of a CSTR with the concentration of output of product as controlled parameter were developed. Proportional Integral (PI) controllers were designed based on 2nd order and FOPDT models of a CSTR using SIMC (Skogestad internal model control), Hagglund and Astrom, and a computational method with 5% overshoot. In all the three tuning methods, the nonlinear model provided better results in terms of various time parameters (Tr, Ty, Ts) and in error analysis (IAE, ITAE and ISE).
461 1 _0(RuTPU)RU\TPU\prd\247369
_x2405-6537
_tResource-Efficient Technologies
_oelectronic scientific journal
_fNational Research Tomsk Polytechnic University (TPU)
_d2015-
463 1 _0(RuTPU)RU\TPU\prd\268664
_tVol. 2, Suppl. 1
_v[P. S71–S75]
_d2016
610 1 _aтруды учёных ТПУ
610 1 _aэлектронный ресурс
610 1 _aПИ-регуляторы
700 0 _aMunna Kumar
701 1 _aSingh
_bR. S.
801 1 _aRU
_b63413507
_c20090623
_gPSBO
801 2 _aRU
_b63413507
_c20180830
_gPSBO
856 4 _uhttp://earchive.tpu.ru/handle/11683/50238
942 _cBK