Porosity-Activity Relationships in Selective Vapour Phase Hydrogenation of Maleic Anhydride on Al-Containing Catalysts

被引:1
作者
Castiglioni, G. L. [1 ]
Guercio, A. [1 ]
Vaccari, A. [1 ]
Lancia, R. [2 ]
机构
[1] Univ Bologna, Dipartimento Chim Ind & Mat, I-40136 Bologna, Italy
[2] Lonza SpA, I-24020 Scanzorosciate, BG, Italy
关键词
maleic anhydride hydrogenation; gamma-butyrolactone; Al-containing catalysts; porosity; selectivity;
D O I
10.1007/BF00486573
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The relationships between physical and catalytic properties for Cu/Zn/Al catalysts in selective vapour phase hydrogenation of maleic anhydride (MA) to gamma-butyrolactone (GBL) was investigated, with particular attention focused on the role of surface area and porosity. The Al-containing catalysts prepared by reduction of cubic spinel-type precursors can be an interesting alternative to Cr-containing catalysts, the use of which are becoming increasingly difficult due to the toxic nature of the spent catalysts. These catalysts gave rise to high productions of GBL, favouring also the formation of tetrahydrofuran (THF) and reducing the amounts of low-cost by-products. In particular, a Cu/Zn/Al = 25:25:50 (atomic ratio %) composition may represent a useful compromise, allowing good yields in GBL to be obtained at lower reaction temperatures, at which the production of by-products is negligible. However, the Al-containing catalysts show higher irreversible adsorption and lower mechanical strength. These unwanted phenomena can be significantly reduced by pressing the catalyst powder without binders at 3.0 tons cm(-2) for 30 min. This treatment gave rise to a decrease of about 25% in both surface area and pore volume, with a significant decrease in micropores and in macropores larger than 150 nm, with a corresponding increase in the pores in the 50-150 nm range. In the catalytic tests with either GBL or a MA/GBL solution, the pressed catalyst showed a decrease in hydrogenation capacity significantly lower than the decrease in surface area, with, however, higher yields in THF and lower formation of unwanted and low-cost by-products (mainly n-butanol and butyric acid). Furthermore, this catalyst exhibited a considerable reduction in crushing and adsorption phenomena, evidencing a positive effect of the pressure treatment on both physical and catalytic properties.
引用
收藏
页码:79 / 84
页数:6
相关论文
共 27 条
  • [21] Ni/Al2O3 catalysts derived from spinel NiAl2O4 for low-temperature hydrogenation of maleic anhydride to succinic anhydride
    Li, Jie
    Ren, Yuanhang
    Yue, Bin
    He, Heyong
    CHINESE JOURNAL OF CATALYSIS, 2017, 38 (07) : 1166 - 1173
  • [22] Vapour-Phase Selective Hydrogenation of γ-Valerolactone to 2-Methyltetrahydrofuran Biofuel over Silica-Supported Copper Catalysts
    Pothu, Ramyakrishna
    Challa, Prathap
    Rajesh, Rajendiran
    Boddula, Rajender
    Balaga, Ravi
    Balla, Putrakumar
    Perugopu, Vijayanand
    Radwan, Ahmed Bahgat
    Abdullah, Aboubakr M.
    Al-Qahtani, Noora
    NANOMATERIALS, 2022, 12 (19)
  • [23] Gas-phase hydrogenation of maleic anhydride to γ-butyrolactone at atmospheric pressure over Cu-CeO2-Al2O3 catalyst
    Yu, Yang
    Guo, Yanglong
    Zhan, Wangcheng
    Guo, Yun
    Wang, Yanqin
    Wang, Yunsong
    Zhang, Zhigang
    Lu, Guanzhong
    JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2011, 337 (1-2) : 77 - 81
  • [24] Intermetallic RNi2Si2 (R = Ca, La, and Y) Catalysts with Electron-Rich Ni Sites for Continuous Flow Selective Hydrogenation of Maleic Anhydride
    Zhong, Ying
    Chen, Xiao
    Liu, Shiyao
    Liu, Huibin
    Hu, Deng
    Lafaye, Gwendoline
    Liang, Changhai
    ACS APPLIED MATERIALS & INTERFACES, 2025, 17 (04) : 6175 - 6187
  • [25] Coupling reaction between ethanol dehydrogenation and maleic anhydride hydrogenation catalyzed by Cu/Al2O3, Cu/ZrO2, and Cu/ZnO catalysts
    Gao, Dezhi
    Feng, Yonghai
    Yin, Hengbo
    Wang, Aili
    Jiang, Tingshun
    CHEMICAL ENGINEERING JOURNAL, 2013, 233 : 349 - 359
  • [26] Gas-phase hydrogenation of maleic anhydride to γ-butyrolactone over Cu-CeO2-Al2O3 catalyst at atmospheric pressure: Effects of the residual sodium and water in the catalyst precursor
    Yu, Yang
    Zhan, Wangcheng
    Guo, Yun
    Lu, Guanzhong
    Adjimi, Souheila
    Guo, Yanglong
    JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2014, 395 : 392 - 397
  • [27] Structure activity relationships of Fe-Co/K-Al2O3 catalysts calcined at different temperatures for CO2 hydrogenation to light olefins
    Numpilai, Thanapa
    Witoon, Thongthai
    Chanlek, Narong
    Limphirat, Wanwisa
    Bonura, Giuseppe
    Chareonpanich, Metta
    Limtrakul, Jumras
    APPLIED CATALYSIS A-GENERAL, 2017, 547 : 219 - 229