Zobrazeno 1 - 10
of 10
pro vyhledávání: '"Romain Lemoine"'
Autor:
Romain Lemoine, John Lee
Publikováno v:
Day 4 Fri, April 26, 2019.
This paper presents a rigorous method to scale rate-time profiles of multi-fractured horizontal wells (MFHW) to a set of reference reservoir and completion properties. Scaling is required for development of accurate production forecasts and typical w
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8c3a5444d142d848abb726f7c0f3fb4f
https://doi.org/10.2118/195338-ms
https://doi.org/10.2118/195338-ms
Autor:
Romain Lemoine, John Lee
Publikováno v:
Day 3 Thu, April 25, 2019.
A common purpose of type wells is to predict the production profiles of multi-fracture horizontal wells (MFHW) in a selected geologically similar area (GSA) in a resource play. This paper presents a unique workflow that leads to type well production
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::b8e0a1e16c98157915dbb246022247bb
https://doi.org/10.2118/195281-ms
https://doi.org/10.2118/195281-ms
Autor:
Badie I. Morsi, Rachid Oukaci, Laurent Sehabiague, Romain Lemoine, Yannick J. Heintz, Arsam Behkish
Publikováno v:
Fuel Processing Technology. 89:322-343
A large number of experimental data points obtained in our laboratory as well as from the literature, covering wide ranges of reactor geometry (column diameter, gas distributor type/open area), physicochemical properties (liquid and gas densities and
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c0ef21a2e1b9dd1a6c88b850cb3d463a
https://doi.org/10.1016/j.fuproc.2007.11.016
https://doi.org/10.1016/j.fuproc.2007.11.016
Autor:
Badie I. Morsi, Laurent Sehabiague, Yannick J. Heintz, Mariela Sanoja, Arsam Behkish, Romain Lemoine, Rachid Oukaci
Publikováno v:
Journal of the Chinese Institute of Chemical Engineers. 39:169-179
A user-friendly simulator based on a comprehensive computer model for slurry bubble column reactors (SBCRs) for Fischer–Tropsch (F–T) synthesis, taking into account the hydrodynamics, kinetics, heat transfer, and mass transfer was developed. The
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d4dd6f567ef36198a78aa1492b4adf0c
https://doi.org/10.1016/j.jcice.2007.11.003
https://doi.org/10.1016/j.jcice.2007.11.003
Publikováno v:
Chemical Engineering Journal. 128:69-84
The holdups of small and large gas bubbles, bubble size distribution and the Sauter-mean bubble diameter were measured for N 2 and He in isoparaffinic organic liquid mixture (Isopar-M) in the absence and presence of Alumina powder under various press
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::14a0f474e5290619ad32dac3af1806cb
https://doi.org/10.1016/j.cej.2006.10.016
https://doi.org/10.1016/j.cej.2006.10.016
Autor:
Romain Lemoine, Badie I. Morsi
Publikováno v:
Chemical Engineering Journal. 114:9-31
A large number of experimental data points (7374) obtained in our laboratory as well as from the literature, covering wide ranges of reactor geometry (reactor diameter and type, impeller diameter and gas distribution scheme), physicochemical properti
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::97be4ae5f2af78cd3a8469f9964f06e3
https://doi.org/10.1016/j.cej.2005.08.015
https://doi.org/10.1016/j.cej.2005.08.015
Publikováno v:
Industrial & Engineering Chemistry Research. 43:6195-6212
The gas holdup (eG), Sauter mean bubble diameter (dS), and bubble size distribution, as well as the volumetric mass-transfer coefficient (kLa), gas−liquid interfacial area (a), and mass-transfer coefficient (kL), of N2 and air were measured in a la
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::73a84414491eb04e568d64c57ffe50bd
https://doi.org/10.1021/ie0400797
https://doi.org/10.1021/ie0400797
Publikováno v:
Chemical Engineering and Processing: Process Intensification. 42:621-643
Almost all available literature correlations to predict the volumetric gas–liquid mass transfer coefficient, kLa in agitated reactors are systems- or operating conditions-dependent. In this study, two back-propagation neural networks (BPNNs), one d
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::abc953890f5432c79233c1add9deb258
https://doi.org/10.1016/s0255-2701(02)00211-8
https://doi.org/10.1016/s0255-2701(02)00211-8
Autor:
Badie I. Morsi, Romain Lemoine
Publikováno v:
International Journal of Chemical Reactor Engineering. 3
The equilibrium gas solubility (C*), gas-holdup (eG), Sauter mean bubble diameter (dS), volumetric mass transfer coefficient (kLa), gas-liquid interfacial area (a) and mass transfer coefficient (kL) of N2, O2 and air were measured in an agitated reac
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::6681684e362c37009100583ccc44c0f8
https://doi.org/10.2202/1542-6580.1166
https://doi.org/10.2202/1542-6580.1166
Publikováno v:
International Journal of Chemical Reactor Engineering. 2
The critical mixing speed for gas entrainment (NCRE), for gas induction (NCRI), induced gas flow rate (QGI) as well as the wavy gas-liquid interfacial area (aWave) of N2 and air were measured in pure toluene and three mixtures of organic liquids (tol
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1c9076e36716aa961992ebac178ccaa2
https://doi.org/10.2202/1542-6580.1155
https://doi.org/10.2202/1542-6580.1155