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Volumn 31, Issue 1, 1998, Pages 111-115

A new merging method of optimal control synthesis for distributed parameter systems

Author keywords

Distributed Parameter Systems; Optimal Control; Tubular Reactor

Indexed keywords

BOUNDARY CONDITIONS; CHEMICAL REACTORS; CONTROL SYSTEM SYNTHESIS; DISTRIBUTED PARAMETER CONTROL SYSTEMS; ENERGY TRANSFER; INTEGRAL EQUATIONS; MASS TRANSFER; MATHEMATICAL MODELS; PARTIAL DIFFERENTIAL EQUATIONS;

EID: 0032002097     PISSN: 00219592     EISSN: None     Source Type: Journal    
DOI: 10.1252/jcej.31.111     Document Type: Article
Times cited : (7)

References (6)
  • 2
    • 51249162789 scopus 로고
    • Comparison of Two Methods of Optimal Control Synthesis: Partial Differential Equation Approach and Integral Equation Approach
    • Choe, Y. S. and K. S. Chang; "Comparison of Two Methods of Optimal Control Synthesis: Partial Differential Equation Approach and Integral Equation Approach," Korean J. of Chem. Eng., 12, 198 (1995)
    • (1995) Korean J. of Chem. Eng. , vol.12 , pp. 198
    • Choe, Y.S.1    Chang, K.S.2
  • 3
    • 11744376811 scopus 로고
    • Modeling of Chemical Reactors-XXIV: Transient Axial Heat and Mass Transfer in Tubular Reactors - The Stability Considerations II
    • Hlavacek, V., H. Hofmann and M. Kubicek; "Modeling of Chemical Reactors-XXIV: Transient Axial Heat and Mass Transfer in Tubular Reactors - The Stability Considerations II," Chem. Eng. Sci., 26, 1629 (1971)
    • (1971) Chem. Eng. Sci. , vol.26 , pp. 1629
    • Hlavacek, V.1    Hofmann, H.2    Kubicek, M.3


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.