Efficient production of renewable hydrocarbon fuels using waste CO2 and green H2 by integrating Fe-based Fischer-Tropsch synthesis and olefin oligomerization

被引:15
作者
Gao, Ruxing [1 ]
Zhang, Leiyu [2 ]
Wang, Lei [1 ]
Zhang, Chundong [2 ]
Jun, Ki-Won [3 ,4 ]
Kim, Seok Ki [3 ,4 ]
Park, Hae-Gu [3 ]
Gao, Ying [1 ]
Zhu, Yuezhao [1 ]
Wan, Hui [2 ]
Guan, Guofeng [2 ]
Zhao, Tiansheng [5 ]
机构
[1] Nanjing Tech Univ, Sch Energy Sci & Engn, Nanjing 211816, Peoples R China
[2] Nanjing Tech Univ, Coll Chem Engn, State Key Lab Mat Oriented Chem Engn, Nanjing 211816, Peoples R China
[3] Korea Res Inst Chem Technol KRICT, Carbon Resources Inst, Gas Separat & Convers Res Grp C1, Yuseong 34114, Daejeon, South Korea
[4] Korea Univ Sci & Technol UST, Adv Mat & Chem Engn, Yuseong 34113, Daejeon, South Korea
[5] Ningxia Univ, State Key Lab High Efficiency Utilizat Coal & Gre, Yinchuan 750021, Ningxia, Peoples R China
基金
新加坡国家研究基金会;
关键词
CO(2 )utilization; Process integration; Fischer-tropsch synthesis; Olefin oligomerization; POWER-TO-LIQUID; HYDROGENATION; CARBON; GAS; CATALYST; STORAGE; ENERGY;
D O I
10.1016/j.energy.2022.123616
中图分类号
O414.1 [热力学];
学科分类号
摘要
Recently, Power-to-Liquids (PtL) and Power-to-Gas (PtG) technologies have been regarded as promising pathways for renewable energy storage and CO2 mitigation. Herein, we newly proposed two PtL/PtG hybrid processes (Cases A and B) by integrating the Fe-based Fischer-Tropsch (F-T) synthesis and olefin oligomerization, to further enhance the production of value-added liquid hydrocarbons. The process modelling and case study were implemented to evaluate their process performances by using Aspen Plus. In addition, the effects of different feeding conditions (i.e., CO/CO2 feeding) and process configurations (i.e., F-T synthesis only or two-stage reactor) were also comparatively analyzed. It is found that both Cases A and B are efficient technologies for converting CO2 into value-added hydrocarbons, and Case A is found to be more beneficial in the aspects of the carbon and thermal efficiencies, and net CO2 reduction. While, Case B is competitive in producing high-value liquid hydrocarbons. Moreover, the options of CO2 feeding and two-stage reactor are more preferable than the options of CO feeding and F-T synthesis only, and both Cases A and B are more competitive in the aspects of syncrude production, thermal efficiency, and CO2 reduction, as compared to the Base cases 1-3. (C) 2022 Elsevier Ltd. All rights reserved.
引用
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页数:10
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