Hydroisomerization of long-chain n-alkanes over Pt/AlSBA-15+zeolite bimodal catalysts

被引:66
作者
Jaroszewska, Karolina [1 ]
Fedyna, Monika [1 ]
Trawczynski, Janusz [1 ]
机构
[1] Wroclaw Univ Sci & Technol, Fac Chem, 7-9 Gdanska, PL-50344 Wroclaw, Poland
关键词
Long-chain n-alkanes; Hydroisomerization; Cold flow properties; AlSBA-15; BEA; MOR; HEXADECANE HYDROISOMERIZATION; DECANE HYDROISOMERIZATION; PRODUCT SELECTIVITY; ALUMINA CATALYSTS; HYBRID CATALYSTS; CETANE NUMBER; METAL CONTENT; BETA-ZEOLITE; SI/AL RATIO; ACID SITES;
D O I
10.1016/j.apcatb.2019.117756
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In this study, the Pt (0.5 wt%) catalysts supported on the bimodal composite materials consisting of AISBA-15 and zeolite (BEA or MOR) were used for hydroisomerization of the long-chain n-alkanes. Consideration was given to the method by which the AISBA-15 and zeolite (20 wt% concentration) were combined: (i) by adding the zeolite to AISBA-15 synthesis gel (Method 1) and (ii) by mechanical mixing the zeolite and AISBA-15 powders (Method 2). The experiments of hydroisomerization of n-hexadecane were carried out using a fixed bed flow reactor system (5 MPa; 260-360 degrees C; WSHV, 3.5 h(-1); H-2:CH, 350:1 Nm(3)/m(3)). It was found that the synthesis of the supports according to Method 1 resulted in a formation of new mesopores in the "zeolitic" phase of A1SBA-15 + zeolite, and also in a moderate acidity of these materials. The catalysts supported on the carriers prepared according to Method 1 exhibited higher activity and isomerization selectivity than these supported on the carriers prepared according to Method 2. The Method 1 yielded the Pt/AlSBA-15 + BEA catalyst displaying the highest isomerization selectivity (together with the highest contribution of monobranched isomers) and the lowest cracking selectivity.
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页数:11
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共 63 条
[41]   Effect of acidity and metal content on the activity and product selectivity for n-decane hydroisomerization and hydrocracking over nickel-tungsten supported on silica-alumina catalysts [J].
Rezgui, Y ;
Guemini, M .
APPLIED CATALYSIS A-GENERAL, 2005, 282 (1-2) :45-53
[42]   Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts [J].
Rezgui, Yacine ;
Guemini, Miloud .
APPLIED CATALYSIS A-GENERAL, 2010, 374 (1-2) :31-40
[43]   Increasing the stability of the Ge-containing extra-large pore ITQ-33 zeolite by post-synthetic acid treatments [J].
Rodriguez-Fernandez, Aida ;
Llopis, Francisco J. ;
Martinez, Cristina ;
Moliner, Manuel ;
Corma, Avelino .
MICROPOROUS AND MESOPOROUS MATERIALS, 2018, 267 :35-42
[44]   Hydroisomerization of n-hexadecane: remarkable selectivity of mesoporous silica post-synthetically modified with aluminum [J].
Sabyrov, Kairat ;
Musselwhite, Nathan ;
Melaet, Gerome ;
Somorjai, Gabor A. .
CATALYSIS SCIENCE & TECHNOLOGY, 2017, 7 (08) :1756-1765
[45]   NiMo/Al2O3 Promoted Hybrid Catalysts of Nanosized Alumina and Beta Zeolite for Hydrocracking with Isomerization [J].
Sakashita, Koji ;
Kimura, Toshiyuki ;
Yoshino, Mami ;
Asaoka, Sachio .
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2011, 54 (05) :320-330
[46]   Evaluation of different reaction strategies for the improvement of cetane number in diesel fuels [J].
Santana, RC ;
Do, PT ;
Santikunaporn, M ;
Alvarez, WE ;
Taylor, JD ;
Sughrue, EL ;
Resasco, DE .
FUEL, 2006, 85 (5-6) :643-656
[47]   Catalysis engineering of bifunctional solids for the one-step synthesis of liquid fuels from syngas: a review [J].
Sartipi, Sina ;
Makkee, Michiel ;
Kapteijn, Freek ;
Gascon, Jorge .
CATALYSIS SCIENCE & TECHNOLOGY, 2014, 4 (04) :893-907
[48]   Catalytic Consequences of Particle Size and Chloride Promotion in the Ring-Opening of Cyclopentane on Pt/Al2O3 [J].
Shi, Hui ;
Gutierrez, Oliver Y. ;
Yang, Hao ;
Browning, Nigel D. ;
Haller, Gary L. ;
Lercher, Johannes A. .
ACS CATALYSIS, 2013, 3 (03) :328-338
[49]   Hydroprocessed vegetable oil as a fuel for transportation sector: A review [J].
Sonthalia, Ankit ;
Kumar, Naveen .
JOURNAL OF THE ENERGY INSTITUTE, 2019, 92 (01) :1-17
[50]   Effect of confinement on the selectivity of hydrocracking [J].
Toulhoat, H ;
Raybaud, P ;
Benazzi, E .
JOURNAL OF CATALYSIS, 2004, 221 (02) :500-509