2015
DOI: 10.1016/j.jngse.2015.06.030
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Optimization and performance improvement of Lekhwair natural gas sweetening plant using Aspen HYSYS

Abstract: This work is licensed under a Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International licence Newcastle University ePrints -eprint.ncl.ac.uk Al-Lagtah NMA, Al-Hasbi S, Onaizi SA. Optimization and performance improvement of Lekhwair natural gas sweetening plant using Aspen HYSYS.

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Cited by 73 publications
(24 citation statements)
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“…In split flow configuration, the needed air to burn the entire acid gas stream burns a portion of feed stream and thereupon the furnace outlet stream temperature is increased. Using the bypass fraction makes the process equal to the process that uses enriched oxygen or pure oxygen . This trend is continued as long as the amount of bypass fraction is excessively high, and then the reaction furnace outlet stream temperature is decreased with further separation.…”
Section: Resultsmentioning
confidence: 99%
“…In split flow configuration, the needed air to burn the entire acid gas stream burns a portion of feed stream and thereupon the furnace outlet stream temperature is increased. Using the bypass fraction makes the process equal to the process that uses enriched oxygen or pure oxygen . This trend is continued as long as the amount of bypass fraction is excessively high, and then the reaction furnace outlet stream temperature is decreased with further separation.…”
Section: Resultsmentioning
confidence: 99%
“…In recent years, very few published articles research on the global optimization of operating conditions to reduce TCEC for the whole high-sulfur gas purification plant. Most optimization studies focus on the subsections, such as GSU (Jassim 2016;Peter et al 2011;Qiu et al 2014;Behroozsarand and Zamaniyan 2011;Al-Lagtah et al 2015), DU (Santos et al 2017;Rouzbahani et al 2014), SRU (Manenti et al 2014;Zarei et al 2016;Adewale et al 2016) and TGTU (Wahedi et al 2015). A typical Iranian gas sweetening plant was simulated by HYSYS v3.1 and optimized by NSGA-II method (Behroozsarand and Zamaniyan 2011).…”
Section: Introductionmentioning
confidence: 99%
“…Three objectives were minimizing of plant energy consumption, amine circulation rate and maximization of carbon dioxide recovery, respectively. Lekhwair natural gas sweetening plant was simulated by HYSYS v7.3 (Al-Lagtah et al 2015). The main operating parameters, lean amine circulation rate, temperature and concentration, were optimized based on sensitivity analysis and keeping the device at its best operating range.…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, if these gas storages were operated without treatments, it would put reservoir engineers as well as the environment at rick. Thus, amine gas sweetening process is the widely used method for acid gas removal (Al-Lagtah et al, 2015). Thus, amine gas sweetening process is the widely used method for acid gas removal (Al-Lagtah et al, 2015).…”
Section: Introductionmentioning
confidence: 99%
“…Thus, urgent solutions are needed to deal with high content of H 2 S. H 2 S removal is the most common way to deal with the acid gas reservoirs (Zhang and Wood, 2015). Additionally, some absorption methods were proposed for H 2 S removal (Abdulrahman and Sebastine, 2013;Adib et al, 2013;Al-Lagtah et al, 2015;Banat et al, 2014). This is also the reason why more than 50% acid gas removal technologies apply the aqueous solutions of alkanolamines.…”
Section: Introductionmentioning
confidence: 99%