New Insights into the Progress on the Isobutane/Butene Alkylation Reaction and Related Processes for High-Quality Fuel Production. A Critical Review

被引:41
作者
Diaz Velazquez, Heriberto [1 ]
Likhanova, Natalya [1 ]
Aljammal, Noor [2 ]
Verpoort, Francis [2 ,3 ]
Martinez-Palou, Rafael [1 ]
机构
[1] Inst Mexicano Petr, Direcc Invest Transformac Hidrocarburos, Mexico City 07730, DF, Mexico
[2] Univ Ghent, Global Campus Songdo, Incheon 21985, South Korea
[3] Wuhan Univ Technol, Lab Organometall Catalysis & Ordered Mat, State Key Lab Adv Technol Mat Synth & Proc, Wuhan 430070, Peoples R China
关键词
METAL-ORGANIC FRAMEWORK; CHLOROALUMINATE IONIC LIQUIDS; SOLID ACID CATALYSTS; H-BETA ZEOLITE; SULFURIC-ACID; ISOBUTANE/2-BUTENE ALKYLATION; DEACTIVATION MECHANISM; INTERFACIAL BEHAVIORS; INTRINSIC KINETICS; GREEN CATALYSTS;
D O I
10.1021/acs.energyfuels.0c02962
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Although research in renewables is growing at a tremendous rate, the world will still be greatly dependent on fossil fuels for at least the first half of this century. In the quest for more efficient and clean fuels, oil refining companies have turned their attention to processes such as reforming and alkylation technologies; in the latter process, isobutane is reacted with butenes and/or propylenes to produce, among others, branched isooctane, which is the main high-octane component of the gasoline pool. The main benefit of this process is the possibility to produce sulfur-free high-octane fuels, so important economic and environmental advantages are foreseen if investments in this area are realized. This Review analyzes and discusses the most recent progress on catalyst technologies, starting from the traditional sulfuric acid process and proceeding to newly emerging catalyst technologies such as solid acid and ionic liquid-based catalysts. We start with basic mechanistic analyses and conclude this Review with the new non-liquid acid-based commercial and emerging technologies for isobutane alkylation. Emphasis is given to the structure-activity relationships and the advantages and disadvantages present in every discussed catalyst material.
引用
收藏
页码:15525 / 15556
页数:32
相关论文
共 170 条
[1]   Pushing the Limits on Metal-Organic Frameworks as a Catalyst Support: NU-1000 Supported Tungsten Catalysts for o-Xylene Isomerization and Disproportionation [J].
Ahn, Sol ;
Nauert, Scott L. ;
Buru, Cassandra T. ;
Rimoldi, Martino ;
Choi, Hyeju ;
Schweitzer, Neil M. ;
Hupp, Joseph T. ;
Farha, Omar K. ;
Notestein, Justin M. .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2018, 140 (27) :8535-8543
[2]   History, Current State, and Prospects for Development of Isobutane Alkylation with Olefins [J].
Akhmadova, Kh Kh ;
Magomadova, M. Kh ;
Syrkin, A. M. ;
Egutkin, N. L. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2019, 53 (04) :643-655
[3]   High-quality fuel distillates produced from oligomerization of light olefin over supported phosphoric acid on H-Zeolite-Y [J].
Al-Kinany, Mohammed C. ;
Al-Drees, Saud A. ;
Al-Megren, Hamid A. ;
Alshihri, Saeed M. ;
Alghilan, Eyad A. ;
Al-Shehri, Feras A. ;
Al-Hamdan, Abdulmohsin S. ;
Alghamdi, Abdullah J. ;
Al-Dress, Sami D. .
APPLIED PETROCHEMICAL RESEARCH, 2019, 9 (01) :35-45
[4]  
Aliyeva M., 2016, THESIS
[5]   Acidic Ionic Liquids [J].
Amarasekara, Ananda S. .
CHEMICAL REVIEWS, 2016, 116 (10) :6133-6183
[6]  
[Anonymous], 1899, fur Niedersachsen
[7]  
[Anonymous], 2016, Hydrocarbon Processing
[8]  
[Anonymous], 2006, OIL GAS J
[9]  
[Anonymous], 2018, HYDROCARBON PROCESSI
[10]  
[Anonymous], 2019, HYDROCARBON PROCESSI