1992
DOI: 10.1016/s1474-6670(17)54018-5
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Integrated Design of Effluent Treatment Systems

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Cited by 9 publications
(16 citation statements)
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“…3) (rd/kd) + 0d. This is then an upper bound on the allowed delay in the process (Walsh, 1993). This is the same value as was obtained in equation (14) using the frequency domain in the case of feedforward control.…”
Section: Step Response Controllability Analysismentioning
confidence: 67%
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“…3) (rd/kd) + 0d. This is then an upper bound on the allowed delay in the process (Walsh, 1993). This is the same value as was obtained in equation (14) using the frequency domain in the case of feedforward control.…”
Section: Step Response Controllability Analysismentioning
confidence: 67%
“…Recall that the expression for dia in (26) compares very well with the numerical closed-loop step responses using PI control (Walsh, 1993). Thus, by comparing 6a in (26) and (28) we see that the open-loop step response analysis is optimistic by a factor n!.…”
Section: Remarksmentioning
confidence: 68%
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“…Another advantage with multiple stages is that one may use successively smaller and smaller control valves, leading to a more precise manipulable variable in the last stage. McMillan and Shinskey both recommend different sized tanks to avoid equal resonance frequencies in the tanks, but this has later been questioned (Walsh, 1993;Faanes and Skogestad, 2000;Faanes and Skogestad, 2003).…”
Section: Introductionmentioning
confidence: 99%