Continuous biodiesel production in a fixed bed reactor packed with anion-exchange resin as heterogeneous catalyst

Bioresource Technology

Volumn 113, Issue , 2012, Pages 19-22

  Ren, Yanbiao ^a   He, Benqiao ^a   Yan, Feng ^a   Wang, Hong ^a   Cheng, Yu ^a   Lin, Ligang ^a   Feng, Yaohui ^a   Li, Jianxin ^a,b  

^a TIANJIN POLYTECHNIC UNIVERSITY   (China)

^b SHANGHAI ADVANCED RESEARCH INSTITUTE   (China)

Author keywords

Biodiesel; Continuous transesterification; D261 anion exchange resin; Fixed bed reactor; Heterogeneous catalyst

Indexed keywords

ANION EXCHANGE RESINS; BIODIESEL PRODUCTION; COMMERCIAL APPLICATIONS; CONTINUOUS PRODUCTION; FEED FLOW RATE; FIXED BED; FIXED BED REACTOR; HETEROGENEOUS CATALYST; IN-SITU; METHYL ESTERS; MOLAR RATIO; N-HEXANE; REACTION TEMPERATURE; RESIDENCE TIME; SOYBEAN OIL;

CATALYSTS; CHEMICAL REACTORS; GLYCEROL; ION EXCHANGE RESINS; METHANOL; TRANSESTERIFICATION;

BIODIESEL;

ANION EXCHANGE RESIN; BIODIESEL; METHANOL; SOYBEAN OIL;

BIOREACTOR; CATALYST; ESSENTIAL OIL; HETEROGENEITY; ION EXCHANGE; METHANOL; RESIN; SOYBEAN;

ARTICLE; BIOCATALYST; BIOFUEL PRODUCTION; FIXED BED REACTOR; PRIORITY JOURNAL; TEMPERATURE;

ANION EXCHANGE RESINS; BIOFUELS; CATALYSIS; MAGNETIC RESONANCE SPECTROSCOPY; SOLVENTS;

GLYCINE MAX;

EID: 84860226948     PISSN: 09608524     EISSN: 18732976     Source Type: Journal    
DOI: 10.1016/j.biortech.2011.10.103     Document Type: Article

References (20)

1. Banerjee A., Chakraborty R. Parametric sensitivity in transesterification of waste cooking oil for biodiesel production - a review. Resour. Conserv. Recycl. 2009, 53:490-497.
2. Chen M., Yortsos Y.C., Rossen W.R. Insights on foam generation in porous media from pore-network studies. Colloids Surf., A 2005, 256:181-189.
3. Edric C., Millicent C., Angelo J., Diamante, Rainier L.C., Raymond Y.R. Internal mass-transfer limitations on the transesterification of coconut oil using an anionic ion exchange resin in a packed bed reactor. Catal. Today 2011, 174:54-58.
4. Enciner J.M., Gonzalez J.F., Rodriguez J.J., Tajedor A. Biodiesels fuel from vegetable oils: transesterification of Cynara cardunculus L. oils with ethanol. Energy Fuels 2002, 16:443-450.
5. Feng Y.H., Zhang A., Li J.X., He B.Q. A continuous process for biodiesel production in a fixed bed reactor packed with cation-exchange resin as heterogeneous catalyst. Bioresour. Technol. 2011, 102:3607-3609.
6. Halim S.F.A., Kamaruddin A.H., Fernando W.J.N. Continuous biosynthesis of biodiesel from waste cooking palm oil in a packed bed reactor: optimization using response surface methodology (RSM) and mass transfer studies. Bioresour. Technol. 2009, 100:710-716.
7. Kalu E.E., Chen K.S., Gedris T. Continuous-flow biodiesel production using slit-channel reactors. Bioresour. Technol. 2011, 102:4456-4461.
8. Kim H., Kang B., Kim M., Park Y., Kim D., Lee J., Lee K. Transesterification of vegetable oil to biodiesel using heterogeneous base catalyst. Catal. Today 2004, 93-95:315-320.
9. Knothe G. Analytical methods used in the production and fuel quality assessment of biodiesel. Trans. ASAE 2001, 44:193-200.
10. Krohn B.J., Mcneff C.V., Yan B. Production of algae-based biodiesel using the continuous catalytic Mcgyan process. Bioresour. Technol. 2011, 102:94-100.
11. Liu Y., Wang L., Yan Y. Biodiesel synthesis combining pre-esterification with alkali catalyzed process from rapeseed oil deodorizer distillate. Fuel Process. Technol. 2009, 90:857-862.
12. Long T., Deng Y., Li G., Gan S., Chen J. Application of N-methylimidizolium functionalized anion exchange resin containing NaOH for production of biodiesel. Fuel Process. Technol. 2011, 92:1328-1332.
13. López D.E., Goodwin J.J.G., Bruce D.A. Transesterification of triacetin with methanol on solid acid and base catalysts. Appl. Catal. A: Gen. 2005, 295:97-105.
14. Marchetti J.M., Miguel V.U., Errazu A.F. Possible methods for biodiesel production. Renew. Sust. Energy Rev. 2007, 11:1300-1311.
15. McNeff C.V., McNeff L.C., Yan B., Nowlan D.T., Rasmussen M., Gyberg A.E., Krohn B.J., Fedie R.L., Hoye T.R. A continuous catalytic system for biodiesel production. Appl. Catal. A: Gen. 2008, 343:39-48.
16. Santacesaria E., Tesser R., Di Serio M., Guida M., Gaetano D., Agreda A.G. Kinetics and mass transfer of free fatty acids esterification with methanol in a tubular packed bed reactor: a key pretreatment in biodiesel production. Ind. Eng. Chem. Res. 2007, 46:5113-5121.
17. Shibasaki-Kitakawa N., Honda H., Kuribayashi H., Toda T., Fukumura T., Yonemoto T. Biodiesel production using anionic ion-exchange resin as heterogeneous catalyst. Bioresour. Technol. 2007, 98:416-421.
18. Srivastava A., Prasad R. Triglycerides-based diesel fuels. Renew. Sust. Energy Rev. 2000, 4:111-133.
19. Tepe O., Dursun A.Y. Combined effects of external mass transfer and biodegradation rates on removal of phenol by immobilized Ralstonia eutropha in a packed bed reactor. J. Hazard. Mater. 2008, 151:9-16.
20. Vicente G., Coteron A., Martinez M., Aracil J. Application of the factorial design of experiments and response surface methodology to optimize biodiesel production. Ind. Crops Prod. 1998, 8:29-35.