Hydrotreatment of the carbohydrate-rich fraction of pyrolysis liquids using bimetallic Ni based catalyst: Catalyst activity and product property relations

被引:22
作者
Yin, Wang [1 ]
Venderbosch, Robertus Hendrikus [2 ]
Alekseeva, Maria V. [3 ]
Figueiredo, Monique Bernardes [1 ]
Heeres, Hans [2 ]
Khromova, Sofia A. [3 ]
Yakovlev, Vadim A. [3 ]
Cannilla, Catia [4 ]
Bonura, Giuseppe [4 ]
Frusteri, Francesco [4 ]
Heeres, Hero Jan [1 ]
机构
[1] Univ Groningen, Dept Chem Engn, Nijenborgh 4, NL-9747 AG Groningen, Netherlands
[2] Biomass Technol Grp BV, Josink Esweg 34, NL-7545 PN Enschede, Netherlands
[3] Boreskov Inst Catalysis, 5 Pr Akad Lavrentieva, Novosibirsk 630090, Russia
[4] CNR ITAE, Ist Tecnol Avanzate Energia Nicola Giordano, Via S Lucia Sopra Contesse, I-98126 Messina, Italy
关键词
Pyrolysis liquids; Pyrolytic sugar; Ni based catalysts; Hydrotreatment; AQUEOUS-PHASE HYDROGENATION; BIO-OIL; SUGAR ALCOHOLS; CU CATALYSTS; BIOMASS; HYDRODEOXYGENATION; CONVERSION; CHEMICALS; KINETICS; FUEL;
D O I
10.1016/j.fuproc.2017.10.006
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The use of novel nickel based catalysts for the catalytic hydrotreatment of pyrolytic sugars, the carbohydrate rich fraction of pine derived pyrolysis liquids, is reported. The catalysts are characterized by a high nickel loading (38 to 57 wt%), promoted by Cu, Pd, and/or Mo and a SiO2 based inorganic matrix. Experiments were carried out at 180 degrees C and 120 bar initial hydrogen pressure (room temperature) in a batch reactor set-up to gain insight in catalyst activity and product properties as a function of the catalyst composition. The most promising catalyst in terms of activity, as measured by the hydrogen uptake during reaction, was the Ni-Mo/SiO2-Al2O3 catalyst whereas the performance of the monometallic Ni/SiO2-Al2O3 catalyst was the lowest. As a result, the product oil obtained by the bimetallic Ni-Mo catalyst showed the highest H/C ratio and the lowest molecular weight of all catalysts tested. A detailed catalyst characterization study revealed that addition of Mo to the Ni catalyst suppresses the agglomeration of nickel nanoparticles during the catalytic hydrotreatment reaction.
引用
收藏
页码:258 / 268
页数:11
相关论文
共 41 条
[1]   Ni-Based Catalysts for the Hydrotreatment of Fast Pyrolysis Oil [J].
Ardiyanti, A. R. ;
Bykova, M. V. ;
Khromova, S. A. ;
Yin, W. ;
Venderbosch, R. H. ;
Yakovlev, V. A. ;
Heeres, H. J. .
ENERGY & FUELS, 2016, 30 (03) :1544-1554
[2]   Catalytic hydrotreatment of fast pyrolysis oil using bimetallic Ni-Cu catalysts on various supports [J].
Ardiyanti, A. R. ;
Khromova, S. A. ;
Venderbosch, R. H. ;
Yakovlev, V. A. ;
Melian-Cabrera, I. V. ;
Heeres, H. J. .
APPLIED CATALYSIS A-GENERAL, 2012, 449 :121-130
[3]   Catalytic hydrotreatment of fast-pyrolysis oil using non-sulfided bimetallic Ni-Cu catalysts on a δ-Al2O3 support [J].
Ardiyanti, A. R. ;
Khromova, S. A. ;
Venderbosch, R. H. ;
Yakovlev, V. A. ;
Heeres, H. J. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2012, 117 :105-117
[4]   Hydrotreatment of wood-based pyrolysis oil using zirconia-supported mono- and bimetallic (Pt, Pd, Rh) catalysts [J].
Ardiyanti, A. R. ;
Gutierrez, A. ;
Honkela, M. L. ;
Krause, A. O. I. ;
Heeres, H. J. .
APPLIED CATALYSIS A-GENERAL, 2011, 407 (1-2) :56-66
[5]  
Ardiyanti A.R., 2013, THESIS
[6]   UPGRADING OF FLASH PYROLYSIS OIL AND UTILIZATION IN REFINERIES [J].
BALDAUF, W ;
BALFANZ, U ;
RUPP, M .
BIOMASS & BIOENERGY, 1994, 7 (1-6) :237-244
[7]   Kinetics of Aqueous-Phase Hydrogenation of Levoglucosan over Ru/C Catalyst [J].
Bindwal, Ankush B. ;
Vaidya, Prakash D. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (50) :17781-17789
[8]   Kinetics of low temperature aqueous-phase hydrogenation of model bio-oil compounds [J].
Bindwal, Ankush B. ;
Bari, Atul H. ;
Vaidya, Prakash D. .
CHEMICAL ENGINEERING JOURNAL, 2012, 207 :725-733
[9]   Stabilized Ni-based catalysts for bio-oil hydrotreatment: Reactivity studies using guaiacol [J].
Bykova, M. V. ;
Ermakov, D. Yu ;
Khromova, S. A. ;
Smirnov, A. A. ;
Lebedev, M. Yu ;
Yakovlev, V. A. .
CATALYSIS TODAY, 2014, 220 :21-31
[10]   Guaiacol hydrodeoxygenation in the presence of Ni-containing catalysts [J].
Bykova M.V. ;
Bulavchenko O.A. ;
Ermakov D.Y. ;
Lebedev M.Y. ;
Yakovlev V.A. ;
Parmon V.N. .
Catalysis in Industry, 2011, 3 (1) :15-22