Process simulation and assessment of a back-up condensate stabilization unit

被引:13
|
作者
Rahmanian, Nejat [1 ]
Bin Ilias, Ilmi [2 ]
Nasrifar, Khashayar [3 ]
机构
[1] Univ Bradford, Fac Engn & Informat, Sch Engn, Bradford BD7 1DP, W Yorkshire, England
[2] Univ Teknol PETRONAS, Dept Chem Engn, Tronoh 31750, Malaysia
[3] Univ Nizwa, Dept Chem & Petrochem Engn, Nizwa, Oman
关键词
Condensate stabilization unit; Aspen HYSYS (R); PRO/II (R); RVP; Sulphur content; EXTRACTIVE DISTILLATION; CO2-ETHANE AZEOTROPE; ABSORPTION; SEPARATION; DESIGN;
D O I
10.1016/j.jngse.2015.06.058
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A simulation was conducted using Aspen HYSYS (R) software for an industrial scale condensate stabilization unit and the results of the product composition from the simulation were compared with the plant data. The results were also compared to the results obtained using PRO/II software. The results show that the simulation is in good agreement with the plant data, especially for medium range hydrocarbons. For hydrocarbons lighter than C-5, the simulation results over predict the plant data while for hydrocarbons heavier than C-9 this trend is reversed. The influences of steam temperature and pressure, as well as feed conditions (flow rate, temperature and pressure) for the product specification (RVP and sulphur content) were also investigated. It was reported that the operating conditions gave rise to the production of off-specification condensate and it was also found that the unit could be utilized within 40-110% of its normal throughput without altering equipment sizing and by the operating parameters. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:730 / 736
页数:7
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