Heat and mass transfer in turbulent flow
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O. T. Hanna; O. C. Sandall; P. R. Mazet
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Article
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1981
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American Institute of Chemical Engineers
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English
β 507 KB
and to indicate potential control difficulties. A similar analysis (Tung and Edgar, 1979) for a fluid catalytic cracker has also highlighted potential difficulties with single loop control. Therefore the dynamic RGA usefully augments the information provided by d static RGA. The analysis can be impl