Abstract
A new control structure for distillation columns, called the 'combined balance structure' is presented. The combined balance structure consists of a linear combination of material balance and energy balance control (conventional control) that can outperform traditional control structures such as LV, DV, ratio structures, etc. Mathematical derivation of this new structure is based on a rigorous transformation technique. The combined balance method unifies the analysis of distillation column control structures and leads to general relative gain array (RGA) relationships that can be used to compare alternative distillation control structures. The importance of inventory control dynamics and the ability of the new optimum combined balance control structure to outperform other conventional control structures are demonstrated by closed-loop comparisons using transfer function representations.
| Original language | English |
|---|---|
| Pages (from-to) | 2159-2168 |
| Number of pages | 10 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 30 |
| Issue number | 9 |
| Publication status | Published - 1991 Sep 1 |
| Externally published | Yes |
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ASJC Scopus subject areas
- Chemical Engineering (miscellaneous)
- Environmental Science(all)
- Polymers and Plastics
Cite this
Combined balance control structure for distillation columns. / Yang, Dae Ryook; Seborg, Dale E.; Mellichamp, Duncan A.
In: Industrial and Engineering Chemistry Research, Vol. 30, No. 9, 01.09.1991, p. 2159-2168.Research output: Contribution to journal › Article
}
TY - JOUR
T1 - Combined balance control structure for distillation columns
AU - Yang, Dae Ryook
AU - Seborg, Dale E.
AU - Mellichamp, Duncan A.
PY - 1991/9/1
Y1 - 1991/9/1
N2 - A new control structure for distillation columns, called the 'combined balance structure' is presented. The combined balance structure consists of a linear combination of material balance and energy balance control (conventional control) that can outperform traditional control structures such as LV, DV, ratio structures, etc. Mathematical derivation of this new structure is based on a rigorous transformation technique. The combined balance method unifies the analysis of distillation column control structures and leads to general relative gain array (RGA) relationships that can be used to compare alternative distillation control structures. The importance of inventory control dynamics and the ability of the new optimum combined balance control structure to outperform other conventional control structures are demonstrated by closed-loop comparisons using transfer function representations.
AB - A new control structure for distillation columns, called the 'combined balance structure' is presented. The combined balance structure consists of a linear combination of material balance and energy balance control (conventional control) that can outperform traditional control structures such as LV, DV, ratio structures, etc. Mathematical derivation of this new structure is based on a rigorous transformation technique. The combined balance method unifies the analysis of distillation column control structures and leads to general relative gain array (RGA) relationships that can be used to compare alternative distillation control structures. The importance of inventory control dynamics and the ability of the new optimum combined balance control structure to outperform other conventional control structures are demonstrated by closed-loop comparisons using transfer function representations.
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UR - http://www.scopus.com/inward/citedby.url?scp=0026223406&partnerID=8YFLogxK
M3 - Article
AN - SCOPUS:0026223406
VL - 30
SP - 2159
EP - 2168
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
SN - 0888-5885
IS - 9
ER -