Renewable production of acrylic acid and its derivative: New insights into the aldol condensation route over the vanadium phosphorus oxides

被引:81
作者
Feng, Xinzhen [1 ]
Sun, Bo [1 ]
Yao, Yao [1 ]
Su, Qin [1 ]
Ji, Weijie [1 ]
Au, Chak-Tong [2 ]
机构
[1] Nanjing Univ, Sch Chem & Chem Engn, Key Lab Mesoscop Chem, Nanjing 210093, Jiangsu, Peoples R China
[2] Hong Kong Baptist Univ, Dept Chem, Kowloon Tong, Hong Kong, Peoples R China
关键词
Acetic acid; Methyl acetate; Formaldehyde; Aldol condensation; Acrylic acid; Vanadium phosphorus oxide; N-BUTANE OXIDATION; MO-V-TE; SELECTIVE OXIDATION; PHOSPHATE CATALYSTS; VPO CATALYSTS; ACETIC-ACID; IN-SITU; METHYL ACETATE; SUPPORTED VPO; PROPANE;
D O I
10.1016/j.jcat.2014.04.005
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
Vanadium phosphorus oxides (VPOs) fabricated by employing poly ethylene glycol (PEG) additive were used as catalysts for efficient conversion of acetic acid (methyl acetate) and formaldehyde to acrylic acid (methyl acrylate). The highest formation rate (19.8 mu mol g(cat)(-1) min(-1)) of desired products (acrylic acid + methyl acrylate) was accomplished over a VPO catalyst comprising mainly vanadyl pyrophosphate ((VO)(2)P2O7) and vanadyl phosphate in 5 form (delta-VOPO4). This catalyst is nearly three times more active than the analogue reported in literature. The VP0 catalyst activated in 1.5% butane-air is superior to that activated in air or nitrogen. Different from the PEG-derived VPO catalysts for n-butane oxidation to maleic anhydride, a better VPO catalyst for the current reaction requires a higher fraction of delta-VOPO4 entity and contains the medium strong acid sites of high density. Through systematic catalyst characterizations and evaluations, an unambiguous correlation between catalyst structure/constitution and performance was established. (C) 2014 Elsevier Inc. All rights reserved.
引用
收藏
页码:132 / 141
页数:10
相关论文
共 64 条
[31]   Amorphous vanadium phosphate catalysts prepared using precipitation with supercritical CO2 as an antisolvent [J].
Hutchings, GJ ;
Lopez-Sanchez, JA ;
Bartley, JK ;
Webster, JM ;
Burrows, A ;
Kiely, CJ ;
Carley, AF ;
Rhodes, C ;
Hävecker, M ;
Knop-Gericke, A ;
Mayer, RW ;
Schlögl, R ;
Volta, JC ;
Poliakoff, M .
JOURNAL OF CATALYSIS, 2002, 208 (01) :197-210
[32]   Effect of Mo on the active sites of VPO catalysts upon the selective oxidation of n-butane [J].
Irusta, S ;
Boix, A ;
Pierini, B ;
Caspani, C ;
Petunchi, J .
JOURNAL OF CATALYSIS, 1999, 187 (02) :298-310
[33]   Effects of ball milling on the doped vanadium phosphorus oxide catalysts [J].
Ji, WJ ;
Xu, LJ ;
Wang, XS ;
Hu, Z ;
Yan, QJ ;
Chen, Y .
CATALYSIS TODAY, 2002, 74 (1-2) :101-110
[34]   Water modification of PEG-derived VPO for the partial oxidation of propane [J].
Jiang, Q. ;
Zhao, J. ;
Li, X. X. ;
Ji, W. J. ;
Zhang, Z. B. ;
Au, C. T. .
APPLIED CATALYSIS A-GENERAL, 2008, 341 (1-2) :70-76
[35]   Structural transformation sequences occurring during the activation of vanadium phosphorus oxide catalysts [J].
Kiely, CJ ;
Burrows, A ;
Hutchings, GJ ;
Bere, KE ;
Volta, JC ;
Tuel, A ;
Abon, M .
FARADAY DISCUSSIONS, 1996, 105 :103-118
[36]   Role of water in the partial oxidation of propane to acrylic acid [J].
Landi, G ;
Lisi, L ;
Volta, JC .
CATALYSIS TODAY, 2004, 91-2 :275-279
[37]   Effect of water on the catalytic behaviour of VPO in the selective oxidation of propane to acrylic acid [J].
Landi, G ;
Lisi, L ;
Volta, JC .
CHEMICAL COMMUNICATIONS, 2003, (04) :492-493
[38]   n-Butane oxidation over VPO catalysts supported on SBA-15 [J].
Li, XK ;
Ji, WH ;
Zhao, J ;
Zhang, ZB ;
Au, CT .
JOURNAL OF CATALYSIS, 2006, 238 (01) :232-241
[39]   Complex metal-oxide catalysts for selective oxidation of propane and derivatives - I. Catalysts preparation and application in propane selective oxidation to acrylic acid [J].
Lin, MM .
APPLIED CATALYSIS A-GENERAL, 2003, 250 (02) :305-318
[40]   Selective oxidation of propane to acrylic acid with molecular oxygen [J].
Lin, MM .
APPLIED CATALYSIS A-GENERAL, 2001, 207 (1-2) :1-16