Esterification of renewable levulinic acid to ethyl levulinate biodiesel catalyzed by highly active and reusable desilicated H-ZSM-5

被引:103
作者
Nandiwale, Kakasaheb Y. [1 ]
Niphadkar, Prashant S. [1 ]
Deshpande, Shilpa S. [1 ]
Bokade, Vijay V. [1 ]
机构
[1] Natl Chem Lab, CSIR, Catalysis & Inorgan Chem Div, Pune 411008, Maharashtra, India
关键词
desilicated H-ZSM-5; levulinic acid; esterification; ethyl levulinate; FREE FATTY-ACID; OIL; PERFORMANCE; ADSORPTION; MEMBRANE; KINETICS; ETHANOL; METHYL; CARBON; ZSM-5;
D O I
10.1002/jctb.4228
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
BACKGROUNDIn the near future, fossil fuel will have limitations in terms of availability and also great concerns over its environmental impact. New routes and related technologies based on renewable feedstocks can overcome most of these problems associated with fossil fuel. Among current biodiesel sources, ethyl levulinate (EL) biodiesel obtained from catalytic esterification of renewable levulinic acid (LA) with ethanol has received a great deal of attention. The use of desilicated H-ZSM-5 (DH-ZSM-5) as heterogeneous acid catalyst for EL biodiesel production in a closed system (under autogeneous pressure) was studied. RESULTSThe effect of reaction parameters such as ethanol to LA molar ratio (4:1 to 10:1), catalyst to LA ratio (0.10-0.25), speed of agitation (100-400rpm), particle size (53-355 mu m), reaction temperature (363-403K) and reaction time (7h) was investigated to maximize LA conversion. CONCLUSIONLevulinic acid conversion reached 95% over DH-ZSM-5 and the catalyst was reusable for up to six cycles. This LA conversion and the catalyst reusability values are higher than others reported in the literature. A pseudo-homogeneous (P-H) kinetic model indicated that reaction rate constants increased with increasing molar ratio, catalyst to LA ratio and reaction temperature. The activation energy decreased from 73.14 to 21.08 kJ mol(-1) when increasing the catalyst to LA ratio from 0.10 to 0.25, which implies a kinetically controlled reaction. (c) 2013 Society of Chemical Industry
引用
收藏
页码:1507 / 1515
页数:9
相关论文
共 27 条
  • [1] Kinetics of esterification of palmitic acid with isopropanol using p-toluene sulfonic acid and zinc ethanoate supported over silica gel as catalysts
    Aafaqi, R
    Mohamed, AR
    Bhatia, S
    [J]. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2004, 79 (10) : 1127 - 1134
  • [2] Synthesis of esters: Development of the rate expression for the Dowex 50 Wx8-400 catalyzed esterification of propionic acid with 1-propanol
    Ali, Sami H.
    Tarakmah, Alia
    Merchant, Sabiha Q.
    Al-Sahhaf, Taher
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (12) : 3197 - 3217
  • [3] Kinetics and mechanism of acetic acid esterification with ethanol on zeolites
    Bedard, Jeremy
    Chiang, Hsu
    Bhan, Aditya
    [J]. JOURNAL OF CATALYSIS, 2012, 290 : 210 - 219
  • [4] Comprehensive kinetic studies of acidic oil continuous esterification by cation-exchange resin in fixed bed reactors
    Cheng, Yu
    Feng, Yaohui
    Ren, Yanbiao
    Liu, Xuan
    Gao, Aoran
    He, Benqiao
    Yan, Feng
    Li, Jianxin
    [J]. BIORESOURCE TECHNOLOGY, 2012, 113 : 65 - 72
  • [5] Removal of free fatty acid in waste frying oil by esterification with methanol on zeolite catalysts
    Chung, Kyong-Hwan
    Chang, Duck-Rye
    Park, Byung-Geon
    [J]. BIORESOURCE TECHNOLOGY, 2008, 99 (16) : 7438 - 7443
  • [6] Chemical routes for the transformation of biomass into chemicals
    Corma, Avelino
    Iborra, Sara
    Velty, Alexandra
    [J]. CHEMICAL REVIEWS, 2007, 107 (06) : 2411 - 2502
  • [7] Ultrasound-Assisted Synthesis of Biodiesel from Palm Fatty Acid Distillate
    Deshmane, Vishwanath G.
    Gogate, Parag R.
    Pandit, Aniruddha B.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (17) : 7923 - 7927
  • [8] Esterification of levulinic acid to n-butyl levulinate over heteropolyacid supported on acid-treated clay
    Dharne, S.
    Bokade, V. V.
    [J]. JOURNAL OF NATURAL GAS CHEMISTRY, 2011, 20 (01): : 18 - 24
  • [9] Levulinic acid esterification with ethanol to ethyl levulinate production over solid acid catalysts
    Fernandes, D. R.
    Rocha, A. S.
    Mai, E. F.
    Mota, Claudio J. A.
    Teixeira da Silva, V.
    [J]. APPLIED CATALYSIS A-GENERAL, 2012, 425 : 199 - 204
  • [10] Microwave-assisted preparation and adsorption performance of activated carbon from biodiesel industry solid reside: Influence of operational parameters
    Foo, K. Y.
    Hameed, B. H.
    [J]. BIORESOURCE TECHNOLOGY, 2012, 103 (01) : 398 - 404