A sensitivity analysis and a comparison of two simulators performance for the process of natural gas sweetening

被引:33
|
作者
Pablo Gutierrez, Juan [1 ]
Benitez, Leonel A. [1 ]
Ruiz, Elisa L. Ale [2 ]
Erdmann, Eleonora [3 ]
机构
[1] Univ Nacl Salta UNSa, Consejo Invest CIUNSa, Inst Invest Ind Quim, UNSa CONICET, Ave Bolivia 5150, RA-4400 Salta, Argentina
[2] Univ Nacl Salta UNSa, Consejo Invest CIUNSa, Fac Ingn, Ave Bolivia 5150, RA-4400 Salta, Argentina
[3] Inst Tecnol Buenos Aires ITBA, Ave Eduardo Madero 399, RA-1106 Buenos Aires, DF, Argentina
关键词
Sweetening; Simulation; Amines; Natural gas; Optimization; CO2; ABSORPTION; ASPEN HYSYS; MODEL; OPTIMIZATION; PLANT;
D O I
10.1016/j.jngse.2016.04.015
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
Chemical processes simulation is an important instrument for the design, optimization and control of industrial plants. Simulation cases can be accomplished with relatively low costs and the absence of risks for the operators. However, the precision of the results depends on the similarity between the simulation performed and the process considered. In this article, two simulators, Aspen Hysys V8.6 and Aspen Plus V8.6, are employed to simulate the process of natural gas sweetening using diethanolamine (DEA). Additionally, a parametric sensitivity analysis is performed to define the optimal operative range for the process. The required data and the conditions of the operating units are taken from a gas conditioning plant in northern Argentina. Finally, a comparison between the block of obtained results from both simulations is also detailed. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:800 / 807
页数:8
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