1992
DOI: 10.1109/16.108231
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Temperature control in a rapid thermal processor

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Cited by 26 publications
(6 citation statements)
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“…For such systems, therefore, traditional model-based MIMO (Multi-Input Multi-Output) control techniques may show limited performance because of their strong model dependency. Such a problem is manifest from the previous studies (Breedijk et al, 1993;Cho et al, 1997;Dilhac et al, 1992;Gyugyi et al, 1992;Schaper et al, 1994;Stuber et al, 1994;Theodoropoulou., 1999).…”
Section: Multivariable Optimal Learning Control Of Multivariable Optimentioning
confidence: 95%
“…For such systems, therefore, traditional model-based MIMO (Multi-Input Multi-Output) control techniques may show limited performance because of their strong model dependency. Such a problem is manifest from the previous studies (Breedijk et al, 1993;Cho et al, 1997;Dilhac et al, 1992;Gyugyi et al, 1992;Schaper et al, 1994;Stuber et al, 1994;Theodoropoulou., 1999).…”
Section: Multivariable Optimal Learning Control Of Multivariable Optimentioning
confidence: 95%
“…Examining the radiative heat transfer terms leads us to consider that an RTP system would be better represented by a linear dynamic model that relates uðtÞ to T 4 w ðtÞ, rather to T w ðtÞ as previously done (Breedijk et al, 1993;Dilhac et al, 1992;Schaper et al, 1994;Stuber et al, 1994;Yang, Lee, & Ahn, 2003). Here T w represents a vector containing the wafer temperatures at the eight locations.…”
Section: Article In Pressmentioning
confidence: 98%
“…All these factors combine to make reliable modeling of the system very difficult (Cho & Gyugyi, 1997). In the presence of significant model errors, traditional feedback control techniques, though successfully applied in some commercial RTP equipments (Peuse, Miner, Yam, & Elia, 1998), may not provide satisfactory temperature tracking performance, as evidenced in some of the previous studies (Breedijk, Edgar, & Trachtenberg, 1993;Dilhac, Ganibal, Bordeneuve, & Nolhier, 1992;Schaper, Moslehi, Sarawat, & Kailath, 1994;Stuber, Trachtenberg, & Edgar, 1994).…”
Section: Introductionmentioning
confidence: 93%
“…For such a surface, the radiosity (total radiant emission per unit area) is represented by (2) where and represent the black-body emissive power and the irradiation (incident radiation energy per unit area), respectively. From this relation, the net radiant heat flow from a surface of area is (3) The net interchange between the two surfaces with area and is represented as (4) where is the view factor from to .…”
Section: A Basic Radiation Equationsmentioning
confidence: 99%