Issue
Korean Journal of Chemical Engineering,
Vol.27, No.5, 1435-1440, 2010
Intrinsic reaction rate and the effects of operating conditions in dimethyl ether synthesis from methanol dehydration
The kinetic behavior of a commercial γ-Al2O3 catalyst for the methanol to dimethyl ether (DME) dehydration reaction has been investigated using a differential fixed bed reactor at the pressure range 1-16 barg within a temperature range of 260-380 ℃. The experimental runs were performed in a wide range of feed to water ratios. The experiments were designed by general full factorial design (GEFD) and a novel rate equation has been developed which exhibited the best fitting with our experimental data. Based on the analysis of variance (ANOVA), the following order of importance for operating conditions was obtained when the objective function is the yield of DME: Temperature>Water % in feed>Pressure. In addition, the optimum operating conditions for the maximum yield of DME, were found at T=380 ℃, P=16 barg and zero wt% of water in the feed.
[References]
  1. Yaripour F, Baghaei F, Schmidt I, Perregaard J, Catal. Commun., 6, 147, 2005
  2. Takeguchi T, Yanagisawa K, Inui T, Inoue M, Appl. Catal. A: Gen., 192(2), 201, 2000
  3. Kim SD, Baek SC, Lee YJ, Jun KW, Kim MJ, Yoo IS, Appl. Catal. A: Gen., 309(1), 139, 2006
  4. Xu MT, Lunsford JH, Goodman DW, Bhattacharyya A, Appl. Catal. A: Gen., 149(2), 289, 1997
  5. Ahn SH, Kim SH, Jung KB, Hahm HS, Korean J. Chem. Eng., 25(3), 466, 2008
  6. Aguayo AT, Erena J, Sierra I, Olazar M, Bilbao J, Catal. Today, 106(1-4), 265, 2005
  7. Lee SB, Cho W, Park DK, Yoon ES, Korean J. Chem. Eng., 23(4), 522, 2006
  8. Yoo YD, Lee SJ, Yun Y, Korean J. Chem. Eng., 24(2), 350, 2007
  9. Shim HM, Lee SJ, Yoo YD, Yun YS, Kim HT, Korean J. Chem. Eng., 26(3), 641, 2009
  10. Takeishi K, Suzuki H, Appl. Catal. A: Gen., 260(1), 111, 2004
  11. Vishwanathan V, Jun KW, Kim JW, Roh HS, Appl. Catal. A: Gen., 276(1-2), 251, 2004
  12. Kumar VS, Padmasri AH, Satyanayana CVV, Reddy IAK, Raju BD, Rao KSR, Catal. Commun., 7, 745, 2006
  13. Mao DS, Yang WM, Xia JC, Zhang B, Song QY, Chen QL, J. Catal., 230(1), 140, 2005
  14. Buelna G, Lin YS, Micro. Meso. Mater., 30, 359, 1999
  15. Buelna G, Lin YS, Micro. Meso. Mater., 42, 67, 2001
  16. Wang ZM, Lin YS, J. Catal., 174(1), 43, 1998
  17. Nie Z, Liu H, Liu D, Ying W, Fang D, J. Nat. Gas Chem., 14, 22, 2005
  18. Bercic G, Levec J, Ind. Eng. Chem. Res., 31, 1035, 1992
  19. Camplo JM, Garcia A, Herencia JF, Luna D, Marinas JM, Romero AA, J. Catal., 151, 307, 1999
  20. Arena F, Dario R, Parmaliana A, Appl. Catal. A: Gen., 170(1), 127, 1998
  21. Montgomery DC, Design and analysis of experiments., John Wiley and Sons, New York, 1996
  22. Dieter GE, Engineering design: A material and processing approach., McGraw-Hill, Inc., New York, 1991
  23. Phadke MS, Quality engineering using robust design., Prentice-Hall, Englewood Cliffs, NJ, 1989