Membrane reactors for biodiesel production with strontium oxide as a heterogeneous catalyst

被引:28
作者
Haponska, Monika [1 ]
Nurra, Claudia [2 ]
Abello, Sonia [2 ]
Makkee, Michiel [3 ]
Salvado, Joan [1 ]
Torras, Caries [1 ]
机构
[1] Univ Rovira & Virgili, Dept Engn Quim, Av Paisos Catalans 26, E-43007 Tarragona, Catalonia, Spain
[2] IREC, Catalonia Inst Energy Res, Marcelli Domingo 2, E-43007 Tarragona, Catalonia, Spain
[3] Delft Univ Technol, Catalysis Engn, Dept Chem Engn, Fac Appl Sci, Van der Maasweg 9, NL-2629 HZ Delft, Netherlands
关键词
Catalytic membrane reactor; Sunflower oil; Biodiesel; Transesterification; Heterogeneous catalyst; SOYBEAN OIL; TRANSESTERIFICATION; PERFORMANCE;
D O I
10.1016/j.fuproc.2018.11.010
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A membrane reactor containing an immobilized heterogeneous catalyst is an alternative for traditional homogeneous-based catalyzed transesterification for biodiesel production. Major problems in homogeneous catalysis are related to catalyst recuperation and soap formation, which can be overcome by using heterogeneous catalysts. Conversion can be increased by a combination of reaction and separation, using membranes with a specific pore size. The aim of this work was to study the performance of different membrane reactors combined with heterogeneous catalysis. The main objectives were: to identify a proper catalyst, to choose the proper immobilization technique, to establish the membrane with the adequate pore size, and to control the reaction and separation process. Amberlysem (R) with acid sites and different types of strontium oxide with basic sites were tested as heterogeneous catalysts. Strontium oxide provided the highest sunflower oil conversion (around 93%) and was easy to immobilize. Two catalytic membrane reactor configurations were investigated, thus confirming the production of several types of methyl esters. The configuration comprising the physical immobilization of the catalyst over the membrane reached a methyl ester yield of > 90 wt%.
引用
收藏
页码:1 / 7
页数:7
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共 32 条
  • [1] Transesterification of soybean oil by PAAc catalytic membrane: Sorption properties and reactive performance for biodiesel production
    Aca-Aca, Gloria
    Loria-Bastarrachea, Maria I.
    Alberto Ruiz-Trevino, E.
    Aguilar-Vega, Manuel
    [J]. RENEWABLE ENERGY, 2018, 116 : 250 - 257
  • [2] Nitroaldol reaction over solid base catalysts
    Akutu, K
    Kabashima, H
    Seki, T
    Hattori, H
    [J]. APPLIED CATALYSIS A-GENERAL, 2003, 247 (01) : 65 - 74
  • [3] A packed bed membrane reactor for production of biodiesel using activated carbon supported catalyst
    Baroutian, Saeid
    Aroua, Mohamed K.
    Raman, Abdul Aziz A.
    Sulaiman, Nik M. N.
    [J]. BIORESOURCE TECHNOLOGY, 2011, 102 (02) : 1095 - 1102
  • [4] Refinery co-processing of renewable feeds
    Bezergianni, Stella
    Dimitriadis, Athanassios
    Kikhtyanin, Oleg
    Kubicka, David
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2018, 68 : 29 - 64
  • [5] Comparative Study of Quick Lime and CaO as Catalysts of Safflower Oil Transesterification
    Camacho, Jesus N.
    Natividad, Reyna
    Galvan Mucino, Gabriel E.
    Garcia-Orozco, Ivan
    Baeza, Ramiro
    Romero, Rubi
    [J]. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2016, 14 (04) : 909 - 917
  • [6] Effect of membrane pore size on the performance of a membrane reactor for biodiesel production
    Cao, Peigang
    Tremblay, Andre Y.
    Dube, Marc A.
    Morse, Katie
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (01) : 52 - 58
  • [7] Kinetics of Canola Oil Transesterification in a Membrane Reactor
    Cao, Peigang
    Tremblay, Andre Y.
    Dube, Marc A.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (05) : 2533 - 2541
  • [8] Performance of a membrane bioreactor for enzymatic transesterification: Characterization and comparison with a batch stirred tank reactor
    Carvalho, CML
    Cunnah, P
    Aires-Barros, MR
    Cabral, JMS
    [J]. BIOCATALYSIS AND BIOTRANSFORMATION, 2000, 18 (01) : 31 - 57
  • [9] Biodiesel synthesis via heterogeneous catalysis using modified strontium oxides as the catalysts
    Chen, Ching-Lung
    Huang, Chien-Chang
    Tran, Dang-Thuan
    Chang, Jo-Shu
    [J]. BIORESOURCE TECHNOLOGY, 2012, 113 : 8 - 13
  • [10] Mixing of viscous immiscible liquids. Part 2: Overemulsification - interpretation and use
    DeRoussel, P
    Khakhar, DV
    Ottino, JM
    [J]. CHEMICAL ENGINEERING SCIENCE, 2001, 56 (19) : 5531 - 5537