Fuzzy Model Identification

碩士 === 國立臺灣大學 === 化學工程學系研究所 === 86 === A simple method for generating a multiple-input/single-outputcrisp-type fuzzy model from observed data is presented in this article.The crisp-type fuzzy mod el is composed of triangular fuzzy partitionsfor inputs and singletons for...

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Bibliographic Details
Main Authors: Hsu, Shuo-Huan, 許碩桓
Other Authors: Chen Cheng-Liang
Format: Others
Language:zh-TW
Published: 1998
Online Access:http://ndltd.ncl.edu.tw/handle/94879299895065269443
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Summary:碩士 === 國立臺灣大學 === 化學工程學系研究所 === 86 === A simple method for generating a multiple-input/single-outputcrisp-type fuzzy model from observed data is presented in this article.The crisp-type fuzzy mod el is composed of triangular fuzzy partitionsfor inputs and singletons for the output. Three steps are proposedin this identification method: initializing phase, growing phase,and refining phase. For a set of observed input/output d ata pairs,the structure and the parameters of a suitable fuzzy model withrequi red accuracy can be determined by a series of algebraiccomputations, and nonli near programming procedure is not needed.Numerical examples are given to demon strate the effectiveness ofthe proposed identification method for modeling sta tic and dynamicdata. The same procedure is also extended to the identificatio n ofTakagi-Sugeno-Kang(TSK) fuzzy model, where some kinds of linear modelare u sed in the consequence part of each fuzzy rule. By introducingthe least squar es algorithm, the TSK modeling is also very easy to implement.Because the fuzz y dynamic model can be simplified as a TSK fuzzy model, the sameprocedure can be used to construct a fuzzy dynamic model.The other focus of this article is how to identify a multiplelinear dynamic model. This type of models is an app lication of theTSK dynamic model. Besides the proposed identification method, twoalternative methods are also suggested: linearization of thenon-linear mat hematical model at several operating points andidentifying a linear model for each operating sub-regime.These methods are demonstrated by three chemical pro cesses:first-order exothermic non-isothermal CSTR, high puritydistillation col umn and neutralization process. A controlsystem design based on the multiple linear model is also proposed.The control system of nonlinear processes design ed based the themultiple linear model may be simpler.