Nonlinear control of a batch ester-interchange reactor = 회분식 에스테르 교환반응기의 비선형 제어

Cited 0 time in webofscience Cited 0 time in scopus
  • Hit : 200
  • Download : 0
Nonlinear control using input/output linearization and sliding mode control are applied to a batch ester-interchange reactor. The batch esterinterchange reaction requires no overshoot of the reaction temperature in the earlier stage of reaction and tight temperature control throughout the reaction to keep the uniform quality of final product and to prevent the variation of the amount of byproduct like diethylene glycol at each batch. The nonlinear controller shows good control performance satisfying these requirements and sliding mode control algorithm is supplimented to improve the robustness against plant-model mismatch.
Advisors
Park, Sun-Wonresearcher박선원researcher
Description
한국과학기술원 : 화학공학과,
Publisher
한국과학기술원
Issue Date
1993
Identifier
68608/325007 / 000911255
Language
eng
Description

학위논문(석사) - 한국과학기술원 : 화학공학과, 1993.2, [ v, 63 p. ]

URI
http://hdl.handle.net/10203/29327
Link
http://library.kaist.ac.kr/search/detail/view.do?bibCtrlNo=68608&flag=dissertation
Appears in Collection
CBE-Theses_Master(석사논문)
Files in This Item
There are no files associated with this item.

qr_code

  • mendeley

    citeulike


rss_1.0 rss_2.0 atom_1.0