نوع مقاله : ترویجی
نویسندگان
1 پژوهشکده توسعه فناوری¬های فرآورش و انتقال گاز، پژوهشگاه صنعت نفت، تهران، ایران، صندوق پستی: 1998-14665
2 پالایشگاه گاز شهیدهاشمی نژاد، سرخس، ایران
3 مدیریت پژوهش و فناوری شرکت ملی گاز ایران، تهران، ایران
4 شرکت مهندسی مشاور نفتون آریا، تهران، ایران
چکیده
کلیدواژهها
عنوان مقاله [English]
نویسندگان [English]
In the present work, a process is developed thatcould separate hydrogen sulfide (H2S) from acid gases with high selectivity. In this process, the main affecting parameters are: type of solvent, process layout and operating conditions. Due to limitation of commercial process simulators, the generic alkanolamines are investigated in this work. By using HYSYS process simulator software, in the first step, among the diisopropanol amine (DIPA) and N-methyldiethanol amine (MDEA) as selective absorbent of hydrogensulfide, the MDEA is selected as solvent. In the next step, by applying the experimental design techniques, the operating conditions regarding to the defined objective function, for three different processes layout are optimized. The optimum results for each case show that the second layout has maximum objective function and selectivity (the objective function is 1.6225 and the selectivity 3.3278) while regarding total energy consumption of the process, third layout with the value of total energy consumption 1.0´108 kCal/h is the best layout.
کلیدواژهها [English]