Applied Instrumentation in the Process Industries: Practical by William G Andrew

By William G Andrew

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22% under optimal conditions: temperature 60 uC; reaction time 10 min; molar ratio of methanol to oil 12 : 1; 1% (w/w of oil) catalyst and minimum recyclability nine times. 5PW12O40 heterogeneous acid catalyst had a higher efficiency for transesterification under microwave irradiation as compared with the conventional method. 3 Chapter 2 Acid–Base Heterogeneous Catalysts Heterogeneous catalysts having both acidic and basic sites have also been investigated which could simultaneously esterify FFA and transesterify TGs to biodiesel.

Rashid and F. Anwar, Energy Fuels, 2008, 22, 1306. ´ . Pe´rez and J. F. Rodrı´guez, 47. A. Casas, C. M. Ferna´ndez, M. J. Ramos, A Fuel, 2010, 89, 650. 48. J. M. Encinar, J. F. Gonza´lez and A. Rodrı´guez-Reinares, Fuel Process. , 2007, 88, 513. Vegetable Oil as a Fuel: Can it be used Directly? 25 49. U. Rashid, F. Anwar and G. Knothe, Fuel Process. , 2009, 90, 1157. 50. W. Xie, H. Peng and L. Chen, Appl. Catal. , 2006, 300, 67. 51. G. J. Suppes, M. P. A. Dasari, E. J. Doskocil, P. J. Mankidy and M.

K. Jacobson, R. Gopinath, L. C. Meher and A. K. Dalai, Appl. Catal. , 2008, 85, 86. 112. A. K. M. G. C. Meher, presented at the IEEE EIC Climate Change Technology Conference, Article No. 4057358, Ottawa, 2006. 113. P. Suarez, A. Z. Plentz, M. S. M. Meneghetti and C. R. Wolf, Quim. , 2007, 30, 667. 114. E. Lotero, Y. E. Lopez, K. Suwannakarn, D. A. Bruce and J. G. Goodwin Jr, Ind. Eng. Chem. , 2005, 44, 5353. 115. R. M. De Almeida, L. K. Noda, N. S. Goncalves, S. M. P. Meneghetti and M. R. Meneghetti, Appl.

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