1998
DOI: 10.1205/026387698524901
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A Rigorous MINLP Model for the Optimal Synthesis and Operation of Utility Plants

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Cited by 143 publications
(71 citation statements)
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“…For a fixed superstructure, Colmenares and Seider (1989) [25] solve an NLP for the integrated design of a utility plant and a chemical plant. The model of Papoulias and Grossmann (1983) [24] is refined by Bruno et al (1998) [26] who provide a MINLP formulation that considers nonlinear characteristics such as steam properties, efficiencies, and gas enthalpies in combustion turbines. Iyer and Grossmann (1998) [27] use a linear multi-period design and operation formulation to account for variable operating conditions.…”
Section: Literature Reviewmentioning
confidence: 99%
“…For a fixed superstructure, Colmenares and Seider (1989) [25] solve an NLP for the integrated design of a utility plant and a chemical plant. The model of Papoulias and Grossmann (1983) [24] is refined by Bruno et al (1998) [26] who provide a MINLP formulation that considers nonlinear characteristics such as steam properties, efficiencies, and gas enthalpies in combustion turbines. Iyer and Grossmann (1998) [27] use a linear multi-period design and operation formulation to account for variable operating conditions.…”
Section: Literature Reviewmentioning
confidence: 99%
“…Bruno et al [72] proposed a superstructure optimization formulated as a MINLP based on the previous work by Papoulias & Grossmann [62]. Manninen & Zhu [73] decomposed the problem into a Master problem that specifies major structural features on a design and flowsheet level, in which an exergy analysis identifies relevant modification options.…”
Section: Case Studymentioning
confidence: 99%
“…In this work we use a superstructure inspired by the previous work of Bruno et al [72]. Figure 2 shows the superstructure, which includes:…”
Section: Case Studymentioning
confidence: 99%
“…For example, the molar enthalpy of a pure ideal gas stream i is calculated with the following equation: 14) where y = T /1000, h ref is associated with the reference value calculating the enthalpy and a i , b i , c i , and d i are constants depending on the substance being considered. All gas streams in the process are treated as mixtures of ideal gases.…”
Section: Working Fluid Propertiesmentioning
confidence: 99%