Solid phosphoric acid catalysts based on mesoporous silica for levoglucosenone production via cellulose fast pyrolysis

被引:23
作者
Santander, Jose A. [1 ]
Alvarez, Mariana [1 ]
Gutierrez, Victoria [2 ]
Volpe, Maria A. [2 ]
机构
[1] UNS, CONICET, INQUISUR, Inst Quim Sur,Chem Dept, Bahia Blanca, Buenos Aires, Argentina
[2] UNS, CONICET, Chem Engn Dept, Planta Piloto Ingn Quim PLAPIQUI, Bahia Blanca, Buenos Aires, Argentina
关键词
solid phosphoric acid; cellulose pyrolysis; levoglucosenone; mesoporous silica; aluminum grafting; NANOPOWDER METAL-OXIDES; NMR; DECOMPOSITION; ALUMINATION; DEHYDRATION; PERFORMANCE; SBA-15; SITES;
D O I
10.1002/jctb.5795
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
BACKGROUND Biochemicals are interesting alternatives for biomass valorization owing to their much higher added value compared to biofuels and energy products. Several methods for the production of valuable chemicals such as levoglucosenone (LGO) via thermochemical processes over solid acid catalysts are being investigated due to their important advantages compared to conventional biomass acid impregnation techniques. The present work explores the synthesis of catalytic materials for the production of this platform molecule. RESULTS Aluminum-loaded SBA-15 mesoporous silica and the corresponding solid phosphoric acid (SPA) catalysts were prepared, characterized by TEM, FTIR, MAS NMR, NH3-TPD, N-2 adsorption, ICP-AES and titration of 'free H3PO4', and tested in cellulose fast pyrolysis. Post-synthesis Al deposition on the silica support produced an increase of bio-oil yield and LGO amount in pyrolysis products. The presence of Al in SPA catalysts led to the formation of aluminum phosphates, decreasing the concentration of H3PO4 species in the surface and therefore the LGO levels. The SPAs presented relatively high LGO levels in the GC-MS detectable liquid products (up to 85 peak area%) which was found to be correlated with the amount of free H3PO4 in the solid catalysts. CONCLUSION Aluminum grafting over SBA-15 is an effective way to increase the selectivity to the target anhydrosaccharide. In SPAs, the presence of Al reduced the easily leachable H3PO4 amount, which is desirable from the point of view of catalyst stability because deactivation is mainly caused by H3PO4 leaching, but also led to lower levels of LGO in bio-oil. (c) 2018 Society of Chemical Industry
引用
收藏
页码:484 / 493
页数:10
相关论文
共 49 条
[1]  
Araujo Lucia Regina Raddi de, 2006, Mat. Res., V9, P181
[2]  
Azimov F., 2012, J. Univ. Chem. Technol. Metall, V47, P333
[3]   Characterization of mesoporous alumina prepared by surface alumination of SBA-15 [J].
Baca, Manuel ;
de la Rochefoucauld, Emmanuel ;
Ambroise, Emmanuelle ;
Krafft, Jean-Marc ;
Hajjar, Redouane ;
Man, Pascal P. ;
Carrier, Xavier ;
Blanchard, Juliette .
MICROPOROUS AND MESOPOROUS MATERIALS, 2008, 110 (2-3) :232-241
[4]   RAMAN AND INFRARED-SPECTRA ON SILICA-GEL EVOLVING TOWARD GLASS [J].
BERTOLUZZA, A ;
FAGNANO, C ;
MORELLI, MA ;
GOTTARDI, V ;
GUGLIELMI, M .
JOURNAL OF NON-CRYSTALLINE SOLIDS, 1982, 48 (01) :117-128
[5]   Dehydration of cellulose to levoglucosenone using polar aprotic solvents [J].
Cao, Fei ;
Schwartz, Thomas J. ;
McClelland, Daniel J. ;
Krishna, Siddarth H. ;
Dumesic, James A. ;
Huber, George W. .
ENERGY & ENVIRONMENTAL SCIENCE, 2015, 8 (06) :1808-1815
[6]  
CARO J, 1989, STUD SURF SCI CATAL, V52, P295
[7]   Catalytic pyrolysis of cellulose using MCM-41 type catalysts [J].
Casoni, Andres I. ;
Nievas, Maria L. ;
Moyano, Elizabeth L. ;
Alvarez, Mariana ;
Diez, Alejandra ;
Dennehy, Mariana ;
Volpe, Maria A. .
APPLIED CATALYSIS A-GENERAL, 2016, 514 :235-240
[8]   EFFECT OF WATER IN THE PERFORMANCE OF THE SOLID PHOSPHORIC-ACID CATALYST FOR ALKYLATION OF BENZENE TO CUMENE AND FOR OLIGOMERIZATION OF PROPENE [J].
CAVANI, F ;
GIROTTI, G ;
TERZONI, G .
APPLIED CATALYSIS A-GENERAL, 1993, 97 (02) :177-196
[9]   Pyrolysis technologies for municipal solid waste: A review [J].
Chen, Dezhen ;
Yin, Lijie ;
Wang, Huan ;
He, Pinjing .
WASTE MANAGEMENT, 2014, 34 (12) :2466-2486
[10]  
Crocker M, 2010, RSC ENERGY ENVIRON S, P1