Techno-economic assessment of small-scale gas to liquid technology to reduce waste flare gas in a refinery plant

被引:16
作者
Kabeh, Kaveh Zayer [1 ]
Teimouri, Aidin [2 ]
Changizian, Sina [3 ]
Ahmadi, P. [4 ]
机构
[1] Shahid Beheshti Univ, Mech & Energy Engn Dept, POB 16765-1719, Tehran, Iran
[2] KN Toosi Univ Technol, Fac Mech Engn Energy Div, POB 19395-19919, Tehran, Iran
[3] Univ Nebraska, Coll Engn, Mech & Mat Dept, Lincoln, NE USA
[4] Istinye Univ, Dept Mech Engn, Fac Engn, Istanbul, Turkiye
关键词
Techno-economic assessment; Gas to liquid (GTL); Microchannel; Flare gas recovery; Fischer-Tropsch synthesis (FTS); FISCHER-TROPSCH; NATURAL-GAS; EFFICIENT UTILIZATION; SWEETENING PROCESS; OPTIMIZATION; ENERGY; PRESSURE; DESIGN; SYNGAS;
D O I
10.1016/j.seta.2022.102955
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The dissemination of toxic substances to the atmosphere and wasting energy by flaring are important challenges for natural gas facilities, and small-scale gas to liquid (GTL) technology can be used as an efficient method to reduce flaring. In this study, a validated model for technical simulation and variable sales prices of GTL products in five different scenarios are used to perform an accurate, comprehensive, and realistic techno-economic assessment of this technology to reduce flaring in the natural gas refinery. The detailed model of gas sweetening, syngas generation and Fischer-Tropsch synthesis (FTS) units have been simulated in the Aspen HYSYS software. The technical results illustrate that the capacity of this plant is 686 barrels per day, and the main products of this plant are diesel and propane. The results demonstrate the economic feasibility of a small-scale GTL plant in all economic conditions unless oil prices decrease significantly in the following years. Based on the obtained results, rising oil price increases the simulated plant's internal rate of return (IRR) to 39.99%. Finally, the sensitivity analysis results indicate that the profitability of this plant can be guaranteed with low oil prices by reducing CapEx to US$ 50,000 per barrel.
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页数:8
相关论文
共 48 条
[11]  
Baxter I, 2013, TRANSFORMATIONAL UPS
[12]   Intensified Fischer-Tropsch synthesis process with microchannel catalytic reactors [J].
Cao, Chunshe ;
Hu, Jianli ;
Li, Shari ;
Wilcox, Wayne ;
Wang, Yong .
CATALYSIS TODAY, 2009, 140 (3-4) :149-156
[13]  
Castelo Branco D, 2008, ANAL IMPLEMENTATION
[14]   The potential of gas-to-liquid technology in the energy market: The case of Qatar [J].
Chedid, R. ;
Kobrosly, M. ;
Ghajar, R. .
ENERGY POLICY, 2007, 35 (10) :4799-4811
[15]  
Da P, 2019, 2SPE195209MS
[16]   Sensitivity analysis for selection of an optimum amine gas sweetening process with minimum cost requirement [J].
Dashti, Sajjad Sharif ;
Shariati, Ahmad ;
Nikou, Mohammad Reza Khosravi .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2015, 10 (05) :709-715
[17]  
EIA, 2021, DIES WHOL PRIC
[18]  
EIA, 2021, PROP WHOL PRIC
[19]  
EIA Biofuels and Emerging Technologies Team, 2013, GTL TECHN ASS SUPP A
[20]  
Farhan Muhamad A., 2020, AIP Conference Proceedings, V2230, DOI 10.1063/5.0002319