On the multiple solutions of the reactive distillation column for production of fuel ethers

被引：9

作者：

Enrique Jairne-Leal, Jose ^{[1
]}

Bonilla-Petriciolet, Adrian ^{[2
]}

Gabriel Segovia-Hernandez, Juan ^{[1
]}

Hernandez, Salvador ^{[1
]}

Hernandez-Escoto, Hector ^{[1
]}

机构：

[1] Univ Guanajuato, Dept Ingn Quim, Div Ciencias Nat & Exactas, Guanajuato 36050, Gto, Mexico

[2] Inst Tecnol Aguascalientes, Dept Ingn Quim, Aguascalientes 20256, Ags, Mexico

来源：

CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION | 2013年 / 72卷

关键词：

Reactive distillation; Input multiplicity; Input-output multiplicity; Fuel ethers; STEADY-STATE MULTIPLICITIES; CONCEPTUAL DESIGN; PREDICTION; OPERATION; SELECTION; IMPACT;

D O I：

10.1016/j.cep.2013.06.001

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：

A systematic study of the operating conditions and parameter sensibility of multiple steady states in a reactive distillation column for production of fuel ethers is presented. The multiplicity analysis is performed using bifurcation diagrams for several scenarios using the process simulator Aspen One Aspen Plus. Our results indicate that the main variables that affect both the presence and behavior of multiple solutions in the reactive distillation column are the reflux ratio, the reboiler duty and the thermal condition in the feed stream. In particular, we have determined that the vapor-liquid stream in the feed has a major influence on the occurrence of this phenomenon and this parameter especially establishes the type of multiplicity that can occur in the reactive distillation column for production of fuel ethers. (C) 2013 Elsevier B.V. All rights reserved.

引用

页码：31 / 41

页数：11

共 33 条

[1] Hardware selection and design aspects for reactive distillation columns. A case study on synthesis of TAME [J].

Baur, R ;

Krishna, R .

CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2002, 41 (05) :445-462

[2] Comparison of equilibrium stage and nonequilibrium stage models for reactive distillation [J].

Baur, R ;

Higler, AP ;

Taylor, R ;

Krishna, R .

CHEMICAL ENGINEERING JOURNAL, 2000, 76 (01) :33-47

[3] Multiple steady states in distillation:: Effect of VL(L)E inaccuracies [J].

Bekiaris, N ;

Güttinger, TE ;

Morari, M .

AICHE JOURNAL, 2000, 46 (05) :955-979

[4] A reactive distillation process for deep hydrodesulfurization of diesel: Multiplicity and operation aspects [J].

Carlos Cardenas-Guerra, J. ;

Lopez-Arenas, Teresa ;

Lobo-Oehmichen, Ricardo ;

Perez-Cisneros, Eduardo S. .

COMPUTERS & CHEMICAL ENGINEERING, 2010, 34 (02) :196-209

[5] Short-Cut Method for the Design of Reactive Distillation Columns [J].

Carrera-Rodriguez, Marcelino ;

Gabriel Segovia-Hernandez, Juan ;

Bonilla-Petriciolet, Adrian .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (18) :10730-10743

[6] Feasibility and synthesis of hybrid reactive distillation systems [J].

Chadda, N ;

Malone, MF ;

Doherty, MF .

AICHE JOURNAL, 2002, 48 (12) :2754-2768

[7] Multiple steady states in reactive distillation: kinetic effects [J].

Chen, FR ;

Huss, RS ;

Doherty, MF ;

Malone, MF .

COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (01) :81-93

[8] Nonlinear control of systems with input and output multiplicities [J].

Chidambaram, M ;

Reddy, GP .

COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 (03) :295-299

[9] Graphical and stage-to-stage methods for reactive distillation column design [J].

Daza, OS ;

Pérez-Cisneros, ES ;

Bek-Pedersen, E ;

Gani, R .

AICHE JOURNAL, 2003, 49 (11) :2822-2841

[10] Conceptual design of single-feed hybrid reactive distillation columns [J].

Dragomir, RM ;

Jobson, M .

CHEMICAL ENGINEERING SCIENCE, 2005, 60 (16) :4377-4395

← 1 2 3 4 →