General framework for the assessment of dynamic resilience. Part II. An application
Abstract
In previous parts of this series methods were developed for the design of plants which are not only optimal at some nominal operating point but which can also deal effectively with disturbances and changes in the operating conditions. These techniques are applied here to synthesize the heat exchanger network and the control structure for a sequence of two exothermic open-loop unstable continuous stirred tank reactors.
- Authors:
- Publication Date:
- Research Org.:
- Imperial Chemical Industries Ltd., Billingham (UK)
- OSTI Identifier:
- 6388111
- Report Number(s):
- DOE/ER/10645-10-Pt.2; CONF-821106-30-Pt.2
ON: DE83009119
- DOE Contract Number:
- AC02-80ER10645
- Resource Type:
- Conference
- Resource Relation:
- Conference: Annual meeting of heat transfer and energy conversion, Los Angeles, CA, USA, 14 Nov 1982; Other Information: Microfiche only, copy does not permit paper copy reproduction
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 32 ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION; CHEMICAL PLANTS; DESIGN; OPERATION; PROCESS CONTROL; CHEMICAL REACTORS; CONTROL SYSTEMS; COMPUTERIZED SIMULATION; HEAT EXCHANGERS; OPTIMIZATION; CONTROL; INDUSTRIAL PLANTS; SIMULATION; 320303* - Energy Conservation, Consumption, & Utilization- Industrial & Agricultural Processes- Equipment & Processes
Citation Formats
Morari, M, Oglesby, M J, and Prosser, I D. General framework for the assessment of dynamic resilience. Part II. An application. United States: N. p., 1982.
Web.
Morari, M, Oglesby, M J, & Prosser, I D. General framework for the assessment of dynamic resilience. Part II. An application. United States.
Morari, M, Oglesby, M J, and Prosser, I D. 1982.
"General framework for the assessment of dynamic resilience. Part II. An application". United States.
@article{osti_6388111,
title = {General framework for the assessment of dynamic resilience. Part II. An application},
author = {Morari, M and Oglesby, M J and Prosser, I D},
abstractNote = {In previous parts of this series methods were developed for the design of plants which are not only optimal at some nominal operating point but which can also deal effectively with disturbances and changes in the operating conditions. These techniques are applied here to synthesize the heat exchanger network and the control structure for a sequence of two exothermic open-loop unstable continuous stirred tank reactors.},
doi = {},
url = {https://www.osti.gov/biblio/6388111},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Mon Feb 01 00:00:00 EST 1982},
month = {Mon Feb 01 00:00:00 EST 1982}
}
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