Zobrazeno 1 - 10
of 28
pro vyhledávání: '"Claude F. Leibovici"'
Publikováno v:
Fluid Phase Equilibria
Fluid Phase Equilibria, Elsevier, 2017, 452, pp.69-73. ⟨10.1016/j.fluid.2017.08.020⟩
Fluid Phase Equilibria, Elsevier, 2017, 452, pp.69-73. ⟨10.1016/j.fluid.2017.08.020⟩
ACL; International audience; In a recent study (D.V. Nichita, C.F. Leibovici, A Rapid and Robust Method for Solving the Rachford-Rice Equation Using Convex Transformations, Fluid Phase Equilib. 353, 2013, 38–49) we have shown that using appropriate
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::69eb19c823d490fd5dcf45610fb6a1d3
https://hal.archives-ouvertes.fr/hal-01815876
https://hal.archives-ouvertes.fr/hal-01815876
Publikováno v:
Chemical Engineering Research and Design. 88:602-605
Two new methods are proposed for solving equations of the form F ( λ ) = ∑ i = 1 n ( a i / ( λ − c i ) ) − 1 = 0 . Both of them are simple, easy to implement, robust and reveal a super-quadratic convergence.
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::be403af4f67b5f728f4abac88a716379
https://doi.org/10.1016/j.cherd.2009.10.012
https://doi.org/10.1016/j.cherd.2009.10.012
Publikováno v:
Fluid Phase Equilibria. 289:94-97
The sensitivity of Boyle temperature to changes in parameters appearing in cubic equations of state and to volume shift is analyzed. Analytical expressions for the Boyle temperature and for the dependency to the shift of the equation of state are giv
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8c52e4ba8605eb3bf73a9594fb4f9d04
https://doi.org/10.1016/j.fluid.2009.11.016
https://doi.org/10.1016/j.fluid.2009.11.016
Publikováno v:
Fluid Phase Equilibria. 286:55-61
When emptying isothermally a supercritical gas container, as already well known, the cumulative production varies linearly with the pressure to compressibility factor ratio. However, the instantaneous production (that is to say, the instantaneous sta
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::3160b754b772ea96bba1b906536d12ba
https://doi.org/10.1016/j.fluid.2009.07.025
https://doi.org/10.1016/j.fluid.2009.07.025
Publikováno v:
Computers & Chemical Engineering. 32:1167-1172
This paper presents a systematic method for optimal lumping of a large number of components in order to minimize the loss of information. In principle, a rigorous composition-based model is preferable to describe a system accurately. However, computa
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::30f2b7120ed7034eb224bf7203847009
https://doi.org/10.1016/j.compchemeng.2007.04.021
https://doi.org/10.1016/j.compchemeng.2007.04.021
Publikováno v:
Fluid Phase Equilibria. 267:127-132
The elegant method proposed by Michelsen [M.L. Michelsen, Calculation of multiphase equilibrium, Comput. Chem. Eng. 18 (1994) 545–550] for solving multiphase Rachford–Rice (RR) equations as a bound constrained minimization is extended to the nega
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::4fe43bf11e92b8ff1076ce4c8c26b796
https://doi.org/10.1016/j.fluid.2008.03.006
https://doi.org/10.1016/j.fluid.2008.03.006
Publikováno v:
Chemical Engineering Communications. 194:648-655
A simple method is proposed for the calculation of any type of P-T curve for the most general case of two-parameter equations of state in the single-phase area. For each component parameter, temperature dependency can be expressed on the basis of any
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::314bc4514ff03cff277c8b5c77cf6bbc
https://doi.org/10.1080/00986440600992768
https://doi.org/10.1080/00986440600992768
Publikováno v:
Fluid Phase Equilibria. 250:1-32
A general analysis is presented to focus on the mathematical and numerical elements of property models for stand-alone results as well as within other calculations. This includes listing all of the equations that constitute a property model and artic
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::01afef3aa68911b9704fe6cc993dcf47
https://doi.org/10.1016/j.fluid.2006.09.010
https://doi.org/10.1016/j.fluid.2006.09.010
Publikováno v:
Fluid Phase Equilibria. 245:71-82
For mixtures with many components, some or most of the components are grouped into pseudo-components in order to reduce the dimensionality of the problem for phase equilibrium calculations, and therefore the computational effort. However, knowing the
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::addaee758b02e486d3bb44850654db68
https://doi.org/10.1016/j.fluid.2006.03.016
https://doi.org/10.1016/j.fluid.2006.03.016
Publikováno v:
Computers & Chemical Engineering
Computers & Chemical Engineering, Elsevier, 2013, 58, pp.378-380. ⟨10.1016/j.compchemeng.2013.07.003⟩
Computers & Chemical Engineering, Elsevier, 2013, 58, pp.378-380. ⟨10.1016/j.compchemeng.2013.07.003⟩
International audience; For the solution of the Frost-Kalkwarf vapor pressure equation (which is both implicit and transcendent), an explicit solution is established in terms of Lambert function. A simple approximation is provided for generating a go
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::0a03f5dfd44327e80522471fdae7a9ad
https://doi.org/10.1016/j.compchemeng.2013.07.003
https://doi.org/10.1016/j.compchemeng.2013.07.003