Application of a fully thermally coupled distillation column for fractionation process in naphtha reforming plant

被引:48
|
作者
Lee, JY
Kim, YH
Hwang, KS
机构
[1] Pusan Natl Univ, Dept Chem Engn, Pusan 609735, South Korea
[2] Dong A Univ, Dept Chem Engn, Pusan 604714, South Korea
关键词
process design; thermally coupled distillation; fractionation process; multi-component distillation;
D O I
10.1016/j.cep.2003.02.001
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
Naphtha reformate is extracted for aromatic compounds and the aromatics are separated into benzene, toluene and xylene in sequence. This separation is conducted using a series of binary-like columns. In this study, the first two columns of the separation process are replaced with a fully thermally coupled distillation column (FTCDC) also known as the Petlyuk column. Though feed of the process contains 18 components, the FTCDC developed for the separation of a ternary system is effectively implemented in the industrial-scale application. A structural design to determine the optimum structure of the column from the minimum tray configuration is utilized, and the minimum tray configuration is found from the stage-to-stage computation with ideal tray efficiency in equilibrium condition. The operating condition to yield a given set of product specifications is found from the HYSYS simulation. The performance of the FTCDC is compared with a conventional two-column process to indicate an energy saving of 13% and the investment cost reduction of 4%. (C) 2003 Elsevier B.V. All rights reserved.
引用
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页码:495 / 501
页数:7
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