Design, simulation and techno-economic analysis of two processes for the conversion of shale gas to ethylene

被引:44
|
作者
Ortiz-Espinoza, Andrea P. [1 ]
Noureldin, Mohamed M. B. [2 ]
El-Halwagi, Mahmoud M. [3 ]
Jimenez-Gutierrez, Arturo [1 ]
机构
[1] Inst Tecnol Celaya, Dept Ingn Quim, Celaya 38010, Gto, Mexico
[2] Texas A&M Univ, Chem Engn Dept, College Stn, TX 77843 USA
[3] King Abdulaziz Univ, Chem & Mat Engn Dept, Jeddah 21589, Saudi Arabia
关键词
Shale gas; Ethylene; Oxidative coupling of methane; Methanol to olefins; Techno-economic analysis; CO2-emissionsa; UOP/HYDRO MTO PROCESS; NATURAL-GAS; OPERATING-CONDITIONS; METHANE; PROPYLENE; ALTERNATIVES; INTEGRATION; REACTORS;
D O I
10.1016/j.compchemeng.2017.05.023
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
Shale gas is being considered as feedstock for the production of major petrochemicals. One such chemical is ethylene. Although the typical production for ethylene is carried out via thermal cracking, alternative processes have been gaining importance recently. Among such alternatives are the Oxidative Coupling of Methane (OCM) and the Methanol to Olefins (MTO) processes. The first one is a direct conversion process while the second one involves several stages. The aim of this work is to carry out an economic, energy and environmental assessment for these two processes. The results show that the MTO process is more profitable under the economic and technical scenario considered here. A sensitivity analysis was conducted to show the shale gas and ethylene prices under which the OCM process would be economically attractive. An analysis on catalyst improvement needed for the OCM process to be profitable is also reported. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:237 / 246
页数:10
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