Clam shell catalyst for continuous production of biodiesel

被引:10
作者
Niju, S. [1 ,2 ]
Begum, K. M. Meera Sheriffa [1 ]
Anantharaman, N. [1 ]
机构
[1] Natl Inst Technol, Dept Chem Engn, Tiruchirappalli 620015, Tamil Nadu, India
[2] PSG Coll Technol, Dept Biotechnol, Coimbatore, Tamil Nadu, India
关键词
Biodiesel; clam shell; continuous process: transesterification; reactive distillation; COOKING PALM OIL; CALCIUM-OXIDE; SOYBEAN OIL; EXCHANGE RESIN; TRANSESTERIFICATION; WASTE; ESTERIFICATION; BATCH; ACID;
D O I
10.1080/15435075.2016.1181074
中图分类号
O414.1 [热力学];
学科分类号
摘要
Continuous flow transesterification of waste frying oil (WFO) with methanol for the biodiesel production was tested in a laboratory scale jacketed reactive distillation (RD) unit packed with clam shell based CaO as solid catalyst. The physiochemical properties of the clam shell catalysts were characterized by X-ray Diffraction (XRD), Brunauer-Emmett-Teller (BET), Scanning Electron Microscopy (SEM), and Energy Dispersive Atomic X-ray Spectrometry (EDAX). The effects of the reactant flow rate, methanol-to-oil ratio, and catalyst bed height were studied to obtain the maximum methyl ester conversion. Reboiler temperature of 65 degrees C was maintained throughout the process for product purification and the system reached the steady state at 7 hr. The experimental results revealed that the jacketed RD system packed with clam shell based CaO showed high catalytic activity for continuous production of biodiesel and a maximum methyl ester conversion of 94.41% was obtained at a reactant flow rate of 0.2 mL/min, methanol/oil ratio of 6:1, and catalyst bed height of 180 mm.
引用
收藏
页码:1314 / 1319
页数:6
相关论文
共 28 条
[21]   Transesterification of palm oil with methanol in a reactive distillation column [J].
Prasertsit, Kulchanat ;
Mueanmas, Chokchai ;
Tongurai, Chakrit .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 70 :21-26
[22]   Continuous biodiesel production in a fixed bed reactor packed with anion-exchange resin as heterogeneous catalyst [J].
Ren, Yanbiao ;
He, Benqiao ;
Yan, Feng ;
Wang, Hong ;
Cheng, Yu ;
Lin, Ligang ;
Feng, Yaohui ;
Li, Jianxin .
BIORESOURCE TECHNOLOGY, 2012, 113 :19-22
[23]   Influence of Co-Solvent on the Production of Biodiesel in Batch and Continuous Process [J].
Sakthivel, S. ;
Halder, Sudipta ;
Gupta, P. D. .
INTERNATIONAL JOURNAL OF GREEN ENERGY, 2013, 10 (08) :876-884
[24]   Synthesis of biodiesel from waste vegetable oil with large amounts of free fatty acids using a carbon-based solid acid catalyst [J].
Shu, Qing ;
Gao, Jixian ;
Nawaz, Zeeshan ;
Liao, Yuhui ;
Wang, Dezheng ;
Wang, Jinfu .
APPLIED ENERGY, 2010, 87 (08) :2589-2596
[25]   AN ECO-FRIENDLY CATALYST DERIVED FROM WASTE SHELL OF SCYLLA TRANQUEBARICA FOR BIODIESEL PRODUCTION [J].
Sivakumar, Pandian ;
Sivakumar, Padmanaban ;
Anbarasu, Kamalakannan ;
Mathiarasi, Ramasamy ;
Renganathan, Sahadevan .
INTERNATIONAL JOURNAL OF GREEN ENERGY, 2014, 11 (08) :886-897
[26]   Esterification of oleic acid in a three-phase, fixed-bed reactor packed with a cation exchange resin catalyst [J].
Son, Sung Mo ;
Kimura, Hiroko ;
Kusakabe, Katsuki .
BIORESOURCE TECHNOLOGY, 2011, 102 (02) :2130-2132
[27]   Combined effects of external mass transfer and biodegradation rates on removal of phenol by immobilized Ralstonia eutropha in a packed bed reactor [J].
Tepe, Ozlem ;
Dursun, Arzu Y. .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 151 (01) :9-16
[28]   Acid-catalyzed esterification of Zanthoxylum bungeanum seed oil with high free fatty acids for biodiesel production [J].
Zhang, Junhua ;
Jiang, Lifeng .
BIORESOURCE TECHNOLOGY, 2008, 99 (18) :8995-8998