2016 International Renewable and Sustainable Energy Conference (IRSEC) 2016
DOI: 10.1109/irsec.2016.7983862
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Optimisation of the energy efficiency and the CO<inf>2</inf> reduction, for the NGL separation

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Cited by 2 publications
(4 citation statements)
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“…Operating parameters vary depending on the separation unit. In our previous work (Ould Brahim & Abderafi, 2016), different pressure values, generally applied in refineries, were tested. For the dethanizer, the pressure was varied from 16 to 23 atm and for the depropanizer, the pressure was varied from 14 to 19 bar.…”
Section: Methods Sensitivity Analysismentioning
confidence: 99%
See 1 more Smart Citation
“…Operating parameters vary depending on the separation unit. In our previous work (Ould Brahim & Abderafi, 2016), different pressure values, generally applied in refineries, were tested. For the dethanizer, the pressure was varied from 16 to 23 atm and for the depropanizer, the pressure was varied from 14 to 19 bar.…”
Section: Methods Sensitivity Analysismentioning
confidence: 99%
“…The use of optimal variables allows a gain in total operating energy equal to 38.37%. To evaluate the performance of the overall LNG separation process, the optimal values of pressure and reflux rate, obtained for the two columns of the Deethanizer and depropanizer in our previous work (Ould Brahim and Abderafi, 2016) and those of the debutanizer found in this study. These values were used to calculate the energy consumed, the operating cost and the concentrations of greenhouse gas emissions, for the studied LNG separation process.…”
Section: Debutanizer Optimization By Gamentioning
confidence: 99%
“…In the combustion of fuels, air is assumed to be in excess to ensure complete combustion, so that no carbon monoxide is formed. The concentration of CO 2 emissions (in kg/s), is related to the amount of fuel burnt, Q Fuel in a heating device [2]. Hence, the optimal value obtained was used to determine CO 2 emissions.…”
Section: Calculation Of Co 2 Emissionsmentioning
confidence: 99%
“…The later is used to separates butane (C 4 ) cuts and lighter components from NGL, typically gasoline. In previous work, modelling and optimization of the distillation column of NGL fraction are studied, especially, for the two first columns [2]. The energy efficiency of the distillation columns was realized, by testing the effects of reflux ratio and column pressure on deethanizer and depropanizer columns.…”
Section: Introductionmentioning
confidence: 99%