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DESIGN AND CONTROL

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Augusto Ocampo Medina

on 27 November 2016

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Transcript of DESIGN AND CONTROL

DESIGN AND CONTROL
OF AN AUTO-REFRIGERATED
ALKYLATION PROCESS
Columns

PROCESS-PRINCIPLES AND CASE STUDIES OF SIMULTANEOUS DESIGN
PROCESS-ASPEN PLUS
DP Column - Design Specs
DIB Column
DP Column - Vary
Augusto Brasil Ocampo Medina
Txy diagrams for (a) propane/isobutane at 220 psia, and (b) isobutane/n-butane at 95 psia.
DIB Column - Design Specs 2
DIB Column - Design Specs 1
Txy diagrams for (a) propane/isobutane at 220 psia, (b) isobutane/n-butane at 95 psia.
DIB Column - Vary 2
Comparation
DIB Column- Vary 1
Txy diagrams for (a) propane/isobutane at 220 psia, (b) isobutane/n-butane at 95 psia.
Txy diagrams for (a) propane/isobutane at 220 psia, (b) isobutane/n-butane at 95 psia.
Txy diagrams for (a) propane/isobutane at 220 psia, (b) isobutane/n-butane at 95 psia.
Txy diagrams for (a) propane/isobutane at 220 psia, (b) isobutane/n-butane at 95 psia.
DP Column
GRACIAS POR SU ATENCION
REFERENCES
1. Mahajanam, R. V., Zheng, A., Douglas, J. M. A shortcut method for control variable section and its application to the butane alkylation process, Ind. Eng. Chem. Res. 2001, 40, 3208.
2. Luyben,W. L. Use of dynamic simulation to converge complex process flowsheets, Chem. Eng. Ed. 2004, 38, 2.
3. Luyben,W. L., Tyreus, B. D., Luyben, M. L. Plantwide Process Control, McGraw-Hill, New York, 1999.
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