On the equivalent dead time

Matsubara, Mitsuru

doi:10.1109/tac.1965.1098179

Cited by 18 publications

(8 citation statements)

References 0 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…We can link the smoothing constant ¬ in the z-transform to Ta in the di erence equation using the EXSMO relationship established by Towill (1977). The EXSMO relationship is based on the Matsuburu (1965) Time Delay Theorem that matches the area under the step response error curve. Speci®cally, ¬ˆ1=…1 ‡ …Ta=¢t)), where ¢t is the sampling interval.…”

Section: The Demand Policymentioning

confidence: 99%

A discrete transfer function model to determine the dynamic stability of a vendor managed inventory supply chain

Disney¹,

Towill²

2002

International Journal of Production Research

215

125

View full text Add to dashboard Cite

Section: The Demand Policymentioning

confidence: 99%

A discrete transfer function model to determine the dynamic stability of a vendor managed inventory supply chain

Disney¹,

Towill²

2002

International Journal of Production Research

215

125

View full text Add to dashboard Cite

“…using the EXSMO relationship established by [17] to link a and ,. This is based on the Matsuburu Time Delay Theorem [18] which matches the area under the step response error curve. The result is the fundamental relationship:…”

Section: Appendix I Developing Elemental Dynamic Building Blocks For mentioning

confidence: 99%

Transfer function analysis of forecasting induced bullwhip in supply chains

Dejonckheere

Disney

Lambrecht

et al. 2002

International Journal of Production Economics

127

View full text Add to dashboard Cite

“…4. The approximate transfer function exhibits the same "equivalent dead time" (Matsubara, 1965) as the original one.…”

Section: Models For Small Chemical Plants and Process Subsystemsmentioning

confidence: 89%

Approximate dynamic models for chemical process systems

Papadourakis¹,

Doherty²,

Douglas³

1989

Ind. Eng. Chem. Res.

View full text Add to dashboard Cite

Modern integrated chemical plants can be viewed as consisting of a number of smaller interconnected subsystems. Approximate dynamic models for both individual process units and subsystems are the necessary tools for preliminary dynamic studies of plantwide operability and control. A variable-order method is presented that can be used to develop simple dynamic models for such systems. The method is successful in retaining the dominant dynamic modes of the process, and examples are given to demonstrate this point.

show abstract

On the equivalent dead time

Cited by 18 publications

References 0 publications

A discrete transfer function model to determine the dynamic stability of a vendor managed inventory supply chain

A discrete transfer function model to determine the dynamic stability of a vendor managed inventory supply chain

Transfer function analysis of forecasting induced bullwhip in supply chains

Approximate dynamic models for chemical process systems

Contact Info

Product

Resources

About