Deactivation kinetics with activity coefficient of the methanol to aromatics process over modified ZSM-5

被引:33
作者
Li, Na [1 ]
Meng, Chen [1 ]
Liu, Dianhua [1 ]
机构
[1] East China Univ Sci & Technol, State Key Lab Chem Engn, 130 Meilong Rd, CN-200237 Shanghai, Peoples R China
基金
国家重点研发计划;
关键词
Methanol to aromatics; Deactivation kinetics; Activity coefficient; TO-OLEFINS PROCESS; HZSM-5 ZEOLITE CATALYST; FLUIDIZED-BED REACTOR; ZEOTYPE CATALYSTS; DIMETHYL ETHER; HYDROCARBONS; CONVERSION; TRANSFORMATION; MODEL; AROMATIZATION;
D O I
10.1016/j.fuel.2018.06.044
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 lumped kinetic model for methanol to aromatics (MTA) process was investigated using modified ZSM-5 industrialized catalyst. The deactivation kinetic behavior of MTA was studied by developing a 5-lump kinetic model to describe the product distributions. The feedstock and products are divided into five lumps by simplifying reaction network, including oxygenates (methanol and dimethyl ether), C-1 (CO, CO2, CH4 and H-2), aliphatic hydrocarbons, light aromatics (C-6-C-8) and heavy aromatics (C9+). The catalytic activity was reflected by activity coefficient a. The deactivation model kinetic parameters were estimated using simplex and nonlinear least squares methods. This model can be used to predict key products and their compositions of MTA industrial process.
引用
收藏
页码:283 / 290
页数:8
相关论文
共 42 条
[1]   Kinetics of Methanol Transformation into Hydrocarbons on a HZSM-5 Zeolite Catalyst at High Temperature (400-550 °C) [J].
Aguayo, Andres T. ;
Mier, Diana ;
Gayubo, Ana G. ;
Gamero, Monica ;
Bilbao, Javier .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (24) :12371-12378
[2]   Conversion of methanol to hydrocarbons over zeolite H-ZSM-5: On the origin of the olefinic species [J].
Bjorgen, Morten ;
Svelle, Stian ;
Joensen, Finn ;
Nerlov, Jesper ;
Kolboe, Stein ;
Bonino, Francesca ;
Palumbo, Luisa ;
Bordiga, Silvia ;
Olsbye, Unni .
JOURNAL OF CATALYSIS, 2007, 249 (02) :195-207
[3]   KINETIC-MODEL FOR METHANOL CONVERSION TO HYDROCARBONS [J].
CHANG, CD .
CHEMICAL ENGINEERING SCIENCE, 1980, 35 (03) :619-622
[4]   Methanol conversion to light olefins over SAPO-34: Reaction network and deactivation kinetics [J].
Chen, D. ;
Grlnvold, A. ;
Moljord, K. ;
Holmen, A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (12) :4116-4123
[5]  
Chen NY, 1979, CHEMINFORM, V10, P123
[6]   Role of water in the kinetic modeling of methanol transformation into hydrocarbons on HZSM-5 zeolite [J].
Gayubo, AG ;
Aguayo, AT ;
Castilla, M ;
Moran, AL ;
Bilbao, J .
CHEMICAL ENGINEERING COMMUNICATIONS, 2004, 191 (07) :944-967
[7]   Reactivation of the HZSM-5 zeolite-based catalyst used in the MTG process [J].
Gayubo, AG ;
Aguayo, AT ;
Benito, PL ;
Landeta, A ;
Castilla, M ;
Bilbao, J .
AICHE JOURNAL, 1997, 43 (06) :1551-1558
[8]   MTG fluidized bed reactor-regenerator unit with catalyst circulation: process simulation and operation of an experimental setup [J].
Gayubo, AG ;
Ortega, JM ;
Aguayo, AT ;
Arandes, JM ;
Bilbao, J .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (16) :3223-3235
[9]   Insights into the Activity and Deactivation of the Methanol-to-Olefins Process over Different Small-Pore Zeolites As Studied with Operando UV-vis Spectroscopy [J].
Goetze, Joris ;
Meirer, Florian ;
Yarulina, Irina ;
Gascon, Jorge ;
Kapteijn, Freek ;
Ruiz-Martinez, Javier ;
Weckhuysen, Bert M. .
ACS CATALYSIS, 2017, 7 (06) :4033-4046
[10]   Unraveling the Reaction Mechanisms Governing Methanol-to-Olefins Catalysis by Theory and Experiment [J].
Hemelsoet, Karen ;
Van der Mynsbrugge, Jeroen ;
De Wispelaere, Kristof ;
Waroquier, Michel ;
Van Speybroeck, Veronique .
CHEMPHYSCHEM, 2013, 14 (08) :1526-1545