CO2 role on the glycerol conversion over catalyst containing CaO-SiO2 doped with Ag and Pt

被引:8
作者
Costa, Jose de Ribamar M. [1 ,2 ]
Santos, Regina C. R. [1 ,3 ]
Coutinho, Lucas P. [1 ]
Silva, Oderlando R. [1 ]
Barros, Helenilson O. [1 ]
Freire, Valder N. [3 ]
Valentini, Antoninho [1 ]
机构
[1] Univ Fed Ceara, Dept Analyt Chem & Phys Chem, Campus Pici, BR-60440554 Fortaleza, CE, Brazil
[2] Univ Fed Maranhao, BR-65915240 Imperatriz, MA, Brazil
[3] Univ Fed Ceara, Dept Phys, Campus Pici, BR-60440554 Fortaleza, CE, Brazil
关键词
Glycerol; CaO; CO2; Dehydration; HYDROGEN-PRODUCTION; BIODIESEL PRODUCTION; LACTIC-ACID; SURFACE-AREA; NI; OXIDE; CU; DEHYDRATION; ETHANOL; AL;
D O I
10.1016/j.cattod.2019.02.009
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Solids with strong base sites of calcium-silica mixed oxides (CaO-SiO2), and zirconia (ZrO2), both doped with platinum (Pt) or argentum (Ag), were synthesized and catalytically evaluated in the dehydration of glycerol for valuable chemical intermediates production. The samples were characterized by X-ray diffraction (XRD), Scanning Electron Microscopy and Energy Dispersive X-ray Spectroscopy (SEM-EDS), Basicity measurements by CO2 temperature programmed desorption (CO2-TPD), thermal analyses (TG/DTA) and N-2 adsorption-desorption isotherms. The effect of two different carrier gas, inert (N-2) or a soft oxidant (CO2) over the activity and selectivity were evaluated in glycerol dehydration for all the samples. The high affinity between Ca and glycerol has effect over the product selectivity, which shows CO2 effect. The promotion with Ag or Pt (0.2 wt%) increase the glycerol conversion and change the product selectivity. The data points out to the hydrogen transfer improving due to the Pt presence. Both, Pt or Ag doping or CO2 addition as the carrier gas may inhibit the acetic acid production, over calcium containing catalyst. The promotion of ZrO2 with Ag or Pt play a less marked effect over the glycerol conversion, under CO2 or N-2.
引用
收藏
页码:199 / 211
页数:13
相关论文
共 80 条
[1]   A thermodynamic analysis of hydrogen production by steam reforming of glycerol [J].
Adhikari, Sushil ;
Fernando, Sandun ;
Gwaltney, Steven R. ;
To, S. D. Filip ;
Bricka, R. Mark ;
Steele, Philip H. ;
Haryanto, Agus .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (14) :2875-2880
[2]   Critical review on the current scenario and significance of crude glycerol resulting from biodiesel industry towards more sustainable renewable energy industry [J].
Ayoub, Muhammad ;
Abdullah, Ahmad Zuhairi .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2012, 16 (05) :2671-2686
[3]   Interaction of carbon dioxide with the surface of zirconia polymorphs [J].
Bachiller-Baeza, B ;
Rodriguez-Ramos, I ;
Guerrero-Ruiz, A .
LANGMUIR, 1998, 14 (13) :3556-3564
[4]  
Bangi B.B., 2011, REV ACETOL APPL PROD, P1135
[6]   CO2 mitigation by carbon nanotube formation during dry reforming of methane analyzed by factorial design combined with response surface methodology [J].
Braga, Tiago P. ;
Santos, Regina C. R. ;
Sales, Barbara M. C. ;
da Silva, Bruno R. ;
Pinheiro, Antonio N. ;
Leite, Edson R. ;
Valentini, Antoninho .
CHINESE JOURNAL OF CATALYSIS, 2014, 35 (04) :514-523
[7]   Correlation between the basicity of Cu-MxOy-Al2O3 (M = Ba, Mg, K or La) oxide and the catalytic performance in the glycerol conversion from adsorption microcalorimetry characterization [J].
Braga, Tiago Pinheiro ;
Essayem, Nadine ;
Valentini, Antoninho .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2017, 129 (01) :65-74
[8]   Synthesis of Cu-MxOy/Al2O3 (M = Fe, Zn, W or Sb) catalysts for the conversion of glycerol to acetol: effect of texture and acidity of the supports [J].
Braga, Tiago Pinheiro ;
Essayem, Nadine ;
Valentini, Antoninho .
RSC ADVANCES, 2015, 5 (113) :93394-93402
[9]   Cu, Fe, or Ni doped molybdenum oxide supported on Al2O3 for the oxidative dehydrogenation of ethylbenzene [J].
Braga, Tiago Pinheiro ;
Pinheiro, Antonio Narcisio ;
Leite, Edson R. ;
dos Santos, Regina Claudia R. ;
Valentini, Antoninho .
CHINESE JOURNAL OF CATALYSIS, 2015, 36 (05) :712-720
[10]   Lactic acid production from glycerol using CaO as solid base catalyst [J].
Chen, Lu ;
Ren, Shoujie ;
Ye, X. Philip .
FUEL PROCESSING TECHNOLOGY, 2014, 120 :40-47