Tailoring MgO-based supported Rh catalysts for purification of gas streams from phenol

被引:60
作者
Polychronopoulou, K. [1 ]
Giannakopoulos, K. [2 ,3 ]
Efstathiou, A. M. [1 ]
机构
[1] Univ Cyprus, Heterogeneous Catalysis Lab, Dept Chem, CY-1678 Nicosia, Cyprus
[2] NCSR Demokritos, Inst Mat Sci, Athens 15310, Greece
[3] NCSR Demokritos, Inst Microelect, Athens 15310, Greece
关键词
Phenol steam reforming; Supported Rh catalysts; MgO-based solid supports; In situ XRD; X-ray photoelectron spectroscopy; High resolution transmission electron microscopy; H-2-TPR; OXYGEN STORAGE CAPACITY; RARE-EARTH-OXIDES; THERMAL-STABILITY; CARBON-DIOXIDE; STEAM GASIFICATION; PARTIAL OXIDATION; PHASE-EQUILIBRIA; H-2; PRODUCTION; FAST PYROLYSIS; NOBLE-METALS;
D O I
10.1016/j.apcatb.2011.10.019
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
The present work is focused on the sal-gel synthesis, characterization and catalytic performance evaluation of novel Mg-Ce-Zr-O-based mixed oxides supported Rh catalysts for the purification of H-2-rich gas streams from phenol through steam reforming in the 575-730 degrees C range. Phenol is used as a model compound of tars, the former being one of the main constituents of tars formed during steam gasification and pyrolysis of biomass. Novel Rh catalysts (0.1 wt%) supported on Mg-Ce-Zr-O-based mixed oxides modified by alkaline-earth, rare earth, and transition metal ions, having the general formula Mg-Ce-Zr-X-O (where X stands for La, Sr, Ba, Ca and Zn) were systematically studied. The physicochemical properties of the catalysts were evaluated using complementary bulk and surface characterization techniques, such as BET, XPS, in situ XRD, TEM/SAED and SEM/EDX. Transient techniques including H-2-TPR,TPD-CO2 and TPD-NH3 were employed in order to characterize redox behavior, surface basicity, and surface acidity of support, respectively. Among the catalysts examined, a 0.1 wt% Rh/40Mg-20Ce-20Zr-20La-O was found to exhibit the highest hydrogen product yield, specific H-2 production rate (mu mol H-2/m(2) min), and the lowest CO/CO2 product ratio (575-730 degrees C), even when compared to a Ni-based commercial steam reforming of tars catalyst. At 655 degrees C, a H-2 yield of similar to 95% and a specific reaction rate of 100 mu mol H-2/m(2) min were obtained for a feed containing 0.5 vol% phenol and 40 vol% H2O at a gas hourly space velocity of similar to 80,000 h(-1). This activity behavior is correlated with the largest concentration of basic sites and labile oxygen species (mu mol/m(2)), and also with the largest acid/base site ratio present in the 40Mg-20Ce-20Zr-20La-O support composition. Steam was also found to be an efficient reagent for the removal of carbonaceous deposits (e.g., CxHy) formed on the catalyst surface during phenol steam reforming. The H/C atom compositional ratio of the carbonaceous deposits was found to depend on reaction temperature. (C) 2011 Elsevier B.V. All rights
引用
收藏
页码:360 / 375
页数:16
相关论文
共 102 条
[1]   Technologies for large-scale gas conversion [J].
Aasberg-Petersen, K ;
Hansen, JHB ;
Christensen, TS ;
Dybkjaer, I ;
Christensen, PS ;
Nielsen, CS ;
Madsen, SELW ;
Rostrup-Nielsen, JR .
APPLIED CATALYSIS A-GENERAL, 2001, 221 (1-2) :379-387
[2]  
[Anonymous], [No title captured]
[3]  
[Anonymous], 1998, BIOMASS GASIFIER TAR
[4]  
Assail M., 1988, B SOC CHIM FR JAN, VI, P106
[5]   IMPROVED STEAM GASIFICATION OF LIGNOCELLULOSIC RESIDUES IN A FLUIDIZED-BED WITH COMMERCIAL STEAM REFORMING CATALYSTS [J].
AZNAR, MP ;
CORELLA, J ;
DELGADO, J ;
LAHOZ, JQ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (01) :1-10
[6]   Surface and reduction energetics of the CeO2-ZrO2 catalysts [J].
Balducci, G ;
Kaspar, J ;
Fornasiero, P ;
Graziani, M ;
Islam, MS .
JOURNAL OF PHYSICAL CHEMISTRY B, 1998, 102 (03) :557-561
[7]   Steam reforming of naphthalene on Ni-Cr/Al2O3 catalysts doped with MgO, TiO2, and La2O3 [J].
Bangala, DN ;
Abatzoglou, N ;
Chornet, E .
AICHE JOURNAL, 1998, 44 (04) :927-936
[8]   Support effect in supported Ni catalysts on their performance for methane partial oxidation [J].
Barbero, J ;
Peña, MA ;
Campos-Martin, JM ;
Fierro, JLG ;
Arias, PL .
CATALYSIS LETTERS, 2003, 87 (3-4) :211-218
[9]   Solid state sintering of lime in presence of La2O3 and CeO2 [J].
Bhattacharya, TK ;
Ghosh, A ;
Tripathi, HS ;
Das, SK .
BULLETIN OF MATERIALS SCIENCE, 2003, 26 (07) :703-706
[10]  
BOROWIECKI T, 1994, STUD SURF SCI CATAL, V88, P537