2017
DOI: 10.1016/j.compchemeng.2017.01.016
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Multi-scale approaches for gas-to-liquids process intensification: CFD modeling, process synthesis, and global optimization

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Cited by 27 publications
(11 citation statements)
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“…For 10 bbl/d (1 bbl = 0.158987 m 3 ) modular microrefinery GtL units to convert wasted natural gas to Fischer‐Tropsch fuels, the investment for 100 units approaches the cost of a single 1000 bbl/d unit, which is 1 million US dollars. [ 102 ] Onel et al [ 108 ] also proposed intensified CH 4 steam methane reforming. They adopted a microchannel reactor and applied a multi‐scale approach that included CFD modelling.…”
Section: Process Intensification and Catalysismentioning
confidence: 99%
“…For 10 bbl/d (1 bbl = 0.158987 m 3 ) modular microrefinery GtL units to convert wasted natural gas to Fischer‐Tropsch fuels, the investment for 100 units approaches the cost of a single 1000 bbl/d unit, which is 1 million US dollars. [ 102 ] Onel et al [ 108 ] also proposed intensified CH 4 steam methane reforming. They adopted a microchannel reactor and applied a multi‐scale approach that included CFD modelling.…”
Section: Process Intensification and Catalysismentioning
confidence: 99%
“…Extended Kalman Filter (EKF) was used as a BB model. Onel et al [41] used a serial GB model for prediction of reactor output composition of steam methane reforming (SMR) microchannel reactor. The non-linear fitting model was used as a BB model.…”
Section: Oil and Gas Processingmentioning
confidence: 99%
“…Application Category Process GB Type Target BB Type [55][56][57] Power plant estimation and control "thermal storage tank", "feed water heater/ heat exchanger" serial "temperature profile and the usable energy stored", "anomaly identification", "irradiation angle" "simultaneous perturbation stochastic approximation", "ANN", "fast recursive algorithm" [40][41][42][43][44] Oil and gas processing "estimation and control", "estimation", "estimation and optimization"…”
Section: Paper Industrymentioning
confidence: 99%
“…Other topics not considered in this perspective paper but could be of interest to the reader are, intensified equipment selection, CFD modeling integrated with process synthesis and optimization, technoeconomic analysis of a specific PI alternative, and optimal reaction concepts for plantwide PI …”
Section: Perspectivesmentioning
confidence: 99%