Decarbonizing the Gas-to-Liquid (GTL) Process Using an Advanced Reforming of Methane Process

被引:5
作者
Ataya, Zeinab [1 ]
Challiwala, Mohamed [1 ,2 ]
Ibrahim, Gasim [1 ,2 ,3 ]
Choudhury, Hanif A. [1 ,2 ]
El-Halwagi, Mahmoud M. [2 ,3 ]
Elbashir, Nimir O. [1 ,2 ]
机构
[1] Texas A&M Univ Qatar, Chem Engn Program, Doha 23874, Qatar
[2] TEES Gas & Fuels Res Ctr, College Stn, TX 77840 USA
[3] Texas A&M Univ, Artie McFerrin Dept Chem Engn, College Stn, TX 77840 USA
来源
ACS ENGINEERING AU | 2023年 / 4卷 / 01期
关键词
dry reforming of methane (DRM); CARGEN; carbonnanotubes (CNTs); autothermal reforming (ATR); gas-to-liquid(GTL); CO2Fix; CO2; SYNGAS; TECHNOLOGIES; INTEGRATION; EMISSIONS; CATALYST; INDUSTRY; ISSUES; WATER;
D O I
10.1021/acsengineeringau.3c00025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The gas-to-liquid (GTL) process is a promising technology for converting natural gas into synthetic fuels and chemicals. However, its high carbon dioxide (CO2) emissions present significant challenges. Methane reforming contributes up to 60% of GTL's CO2 emissions, necessitating decarbonization. Dry reforming of methane (DRM) shows potential for CO(2 )conversion. Still, it faces challenges such as high energy requirements, catalyst deactivation, and an incompatible hydrogen-to-carbon monoxide (H-2/CO) ratio for GTL processing, requiring extensive research. A previous study proposed a two-reactor system known as CARGEN that co-produces solid carbon (in the form of multiwalled carbon nanotubes [MWCNTs]) and syngas, reducing CO2 emissions by 40% compared to the benchmark autothermal reforming (ATR) process through life cycle assessment (LCA) studies. This paper presents a comprehensive simulation of the advanced DRM process used to retrofit an existing ATR-based GTL plant-initially, a 50,000 bbl./day ATR-based GTL plant is simulated. The advanced reformer process replaces ATR through retrofitting. Comparative analysis shows a remarkable 73% reduction in net CO2 emissions and the potential coproduction of 243 kg of MWCNTs per barrel of syncrude, equivalent to 12,150 tons/day of MWCNTs. However, the advanced reformer-based GTL plant requires 61% more natural gas feedstock while utilizing 79% less oxygen than the ATR-based plant. Furthermore, a separate techno-economic analysis examines the advanced reformer-based GTL plant based on a calculation for 13,100 tons/day of CO2 feedstock to co-produce 3,277 tons/day of MWCNTs and 50,000 barrels/day of syncrude. This analysis, considering a 25% tax rate, 25-year plant life, and zero salvage value, demonstrates an attractive 10-year payback period at selling prices of 80 USD/bbl. for syncrude and 10 USD/kg for MWCNTs. These results provide a process system-level perspective, showcasing the advanced reformer-based GTL plant (CARGEN Process) as an effective solution for low-carbon GTL production.
引用
收藏
页码:99 / 111
页数:13
相关论文
共 45 条
[1]  
Aasberg-petersen B. K., LARGE SCALE METHANOL
[2]   Optimization Approach to the Reduction of CO2 Emissions for Syngas Production Involving Dry Reforming [J].
Afzal, Shaik ;
Sengupta, Debalina ;
Sarkar, Amitava ;
El-Halwagi, Mahmoud ;
Elbashir, Nimir .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2018, 6 (06) :7532-7544
[3]   Syngas production through dry reforming: A review on catalysts and their materials, preparation methods and reactor type [J].
Alipour, Zahra ;
Borugadda, Venu Babu ;
Wang, Hui ;
Dalai, Ajay K. .
CHEMICAL ENGINEERING JOURNAL, 2023, 452
[4]  
[Anonymous], 2020, CHEM ENG PROG, V116, P9
[5]  
[Anonymous], 2023, AIR POLLUT CONTROL
[6]  
[Anonymous], 2023, ORYX GTL
[7]  
[Anonymous], 1981, 1 UK NATL FLAP REGIS
[8]   Catalyst design for dry reforming of methane: Analysis review [J].
Aramouni, Nicolas Abdel Karim ;
Touma, Jad G. ;
Abu Tarboush, Belal ;
Zeaiter, Joseph ;
Ahmad, Mohammad N. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 82 :2570-2585
[9]   Methane Conversion to Syngas for Gas-to-Liquids (GTL): Is Sustainable CO2 Reuse via Dry Methane Reforming (DMR) Cost Competitive with SMR and AIR Processes? [J].
Baltrusaitis, Jonas ;
Luyben, William L. .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2015, 3 (09) :2100-2111
[10]   Simulation, integration, and economic analysis of gas-to-liquid processes [J].
Bao, Buping ;
El-Halwagi, Mahmoud M. ;
Elbashir, Nimir O. .
FUEL PROCESSING TECHNOLOGY, 2010, 91 (07) :703-713