Low-Olefin Production Process Based on Fischer-Tropsch Synthesis: Process Synthesis, Optimization, and Techno-Economic Analysis

被引:17
|
作者
Liu, Yuping [1 ]
Kamata, Hiroyuki [1 ]
Ohara, Hiroaki [1 ]
Izumi, Yoshinori [1 ]
Ong, Daniel Sze Wei [2 ]
Chang, Jie [2 ]
Poh, Chee Kok [2 ]
Chen, Luwei [2 ]
Borgna, Armando [2 ]
机构
[1] IHI Corp, Chem Engn Dept, Prod Dev Ctr, Yokohama, Kanagawa 2358501, Japan
[2] ASTAR, Inst Chem & Engn Sci, Singapore 627833, Singapore
关键词
LIQUID TRANSPORTATION FUELS; SYNTHESIS GAS; NATURAL-GAS; DIRECT CONVERSION; CATALYSTS; METHANE; TECHNOLOGY; SYNGAS; COAL; CO2;
D O I
10.1021/acs.iecr.0c00542
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A low-olefin production process was developed with natural gas as the feedstock. The proposed process directly generates low olefins based on the Fischer-Tropsch synthesis reaction. Techno-economic assessments were conducted to evaluate the economic aspects of the developed process, whereby data were compared to that of the counterpart gas-to-liquid process. Results showed that the Fischer-Tropsch to olefins process has good economic prospects. This work provides a feasible approach for a low-olefin production process through process synthesis and optimization. Input chilling utilities could be reduced by 45% compared to that before the exergy recuperation and heat integration, while the heating utilities could be reduced to 0 MMBtu/h. Effects of catalyst's selectivity to low olefins on the economic performance of the proposed process were also analyzed.
引用
收藏
页码:8728 / 8739
页数:12
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