1997
DOI: 10.1016/s0378-3812(97)00151-9
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The isoenergetic-isochoric flash

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Cited by 41 publications
(24 citation statements)
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“…Furthermore, Gopal and Biegler (1997) assume perfect pressure control and specify the temperature trajectory in the drum, what results in a much simpler version of the dynamic flash problem. The articles of Saha and Carroll (1997) and Michelsen (1999) are based on UVN flash formulations that use nested-loops since pressure is an iteration variable. This has the disadvantage of requiring the solution of the EOS to obtain the molar volume of each phase in every iteration.…”
Section: Introductionmentioning
confidence: 99%
“…Furthermore, Gopal and Biegler (1997) assume perfect pressure control and specify the temperature trajectory in the drum, what results in a much simpler version of the dynamic flash problem. The articles of Saha and Carroll (1997) and Michelsen (1999) are based on UVN flash formulations that use nested-loops since pressure is an iteration variable. This has the disadvantage of requiring the solution of the EOS to obtain the molar volume of each phase in every iteration.…”
Section: Introductionmentioning
confidence: 99%
“…This first example [3] consists in filling a vessel with pure nitrogen. The vessel has inlet and outlet connections.…”
Section: Examplementioning
confidence: 99%
“…Therefore, it is interesting to develop a framework that can be used to simulate the dynamics of separation vessels with phases modeled by EOS. Few papers on vessel dynamics discuss the use of EOS [3][4][5]. This is by no means a trivial extension of dynamic models based on simpler assumptions about phase behavior because: -vapor-liquid equilibrium calculations tend to be more difficult at high pressures than at low pressures, because of the larger departure from ideal phase behavior and the proximity of the mixture critical point; -depending on calculation algorithm and problem specifications, it may be necessary to solve the equation of state to find the molar volume at a given condition of temperature, pressure and system composition.…”
Section: Introductionmentioning
confidence: 99%
“…It is usual to avoid numerical entropy maximization because the EOS normally used for chemical process design give thermodynamic properties as explicit functions of temperature (instead of internal energy), volume, and number of moles. Saha and Carroll [11] simulated vessel dynamics with equations of state using an algorithm with nested loops to solve the algebraic phase equilibrium equations. Gonçalves et al [12] used a single loop approach to solve the algebraic equations based on a reformulation of the UVn flash equations using a framework originally proposed by Michelsen [13].…”
Section: Introductionmentioning
confidence: 99%