Effect of Metal-Acid Balance on Hydroprocessed Renewable Jet Fuel Synthesis from Hydrocracking and Hydroisomerization of Biohydrogenated Diesel over Pt-Supported Catalysts

被引:55
作者
Hengsawad, Tepin [1 ]
Srimingkwanchai, Chayasari [1 ]
Butnark, Suchada [2 ]
Resasco, Daniel E. [3 ]
Jongpatiwut, Siriporn [1 ,4 ]
机构
[1] Chulalongkorn Univ, Petr & Petrochem Coll, Bangkok 10330, Thailand
[2] PTT Publ Co Ltd, PTT Res & Technol Inst, Ayutthaya 13170, Thailand
[3] Univ Oklahoma, Sch Chem Biol & Mat Engn, Norman, OK 73019 USA
[4] Chulalongkorn Univ, Ctr Excellence Petrochem & Mat Technol, Bangkok 10330, Thailand
关键词
N-HEXADECANE HYDROISOMERIZATION; PT/ZEOLITE CATALYSTS; ALUMINA CATALYSTS; HYDROCARBON FUELS; SILICA-ALUMINA; BETA ZEOLITES; VEGETABLE-OIL; JATROPHA OIL; ISOMERIZATION; DECANE;
D O I
10.1021/acs.iecr.7b04711
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The development of Pt-supported catalysts for a selective hydrocracking and hydroisomerization of biohydrogenated diesel (BHD, n-C15-C18) to hydroprocessed renewable jet (HRJ) fuel (C9-C14) was investigated. The different acidic supports (i.e., HY zeolite with SiO2/Al2O3 ratios of 5.5 and 100 and amorphous silica-alumina supports) loaded with 0.5 wt % Pt content were prepared and tested for the catalytic conversion of BI-ID to HRJ fuel. The Pt supported on HY zeolite with SiO2/Al2O3 ratio of 100 denoted as Pt/HY(100) catalyst exhibited the highest jet fuel yield with high branched isomers due to its good balance between metal and acid function. The effects of the reaction temperature, reaction pressure, and liquid hourly space velocity (LHSV) on the hydrocracking and hydroisomerization performance were studied over Pt/HY(100) catalyst. The jet fuel yield was obtained at maximum value of 33 wt % at 310 degrees C, 450 psig, LHSV of 1.0 h(-1), and H-2/BHD molar ratio of 30. A stability test was also conducted over Pt/HY(100) catalyst for 160 h. No significant change in the catalytic activity and selectivity during the test was observed, indicating the high stability of the Pt/HY(100) catalyst.
引用
收藏
页码:1429 / 1440
页数:12
相关论文
共 80 条
[1]   Recent advances and future aspects in the selective isomerization of high n-alkanes [J].
Akhmedov, Vagif M. ;
Al-Khowaiter, Soliman H. .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2007, 49 (01) :33-139
[2]   Hydroisomerization and hydrocracking of alkanes - Influence of the balance between acid and hydrogenating functions on the transformation of n-decane on PtHY catalysts [J].
Alvarez, F ;
Ribeiro, FR ;
Perot, G ;
Thomazeau, C ;
Guisnet, M .
JOURNAL OF CATALYSIS, 1996, 162 (02) :179-189
[3]   Challenges and opportunities of enhancing cold flow properties of biodiesel via heterogeneous catalysis [J].
Anwar, Adeel ;
Garforth, Arthur .
FUEL, 2016, 173 :189-208
[4]   Catalytic Hydrocracking of Fresh and Used Cooking Oil [J].
Bezergianni, Stella ;
Voutetakis, Spyros ;
Kalogianni, Aggeliki .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (18) :8402-8406
[5]   Hydrocracking of vacuum gas oil-vegetable oil mixtures for biofuels production [J].
Bezergianni, Stella ;
Kalogianni, Aggeliki ;
Vasalos, Iacovos A. .
BIORESOURCE TECHNOLOGY, 2009, 100 (12) :3036-3042
[6]   Aviation gas turbine alternative fuels: A review [J].
Blakey, Simon ;
Rye, Lucas ;
Wilson, Christopher Willam .
PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2011, 33 :2863-2885
[7]  
Blommel PG, 2008, INT SUGAR J, V110, P672
[8]   Hydroisomerization and hydrocracking of long chain n-alkanes on Pt/amorphous SiO2-Al2O3 catalyst [J].
Calemma, V ;
Peratello, S ;
Perego, C .
APPLIED CATALYSIS A-GENERAL, 2000, 190 (1-2) :207-218
[9]   Middle distillates from hydrocracking of FT waxes: Composition, characteristics and emission properties [J].
Calemma, Vincenzo ;
Gambaro, Chiara ;
Parker, Wallace O., Jr. ;
Carbone, Rosa ;
Giardino, Roberto ;
Scorletti, Pietro .
CATALYSIS TODAY, 2010, 149 (1-2) :40-46
[10]  
Serrano-Ruiz JC, 2012, ENERG ENVIRON SCI, V5, P5638, DOI [10.1039/c1ee02418c, 10.1039/C1EE02418C]