000 02243nam a2200265 a 4500
001 vtls000075904
003 KUKTEM
005 20251114204551.0
008 131107t2013 my da f m 000 0 eng d
020 _aTHE0003563(Local)
039 9 _a201905152114
_bzulaiha
_c201311131648
_dnabilah
_y201311071528
_znabilah
040 _aUMP
090 _aTJ265 .Q77 2013 rs Bc.
100 0 _aQurratuaini Hassanusi
245 1 0 _aThermodynamic study of propane dehydrogenation into propylene /
_cQurratuaini Hassanusi
260 _aKuantan, Pahang :
_bUMP,
_c2013
300 _axi, 48 p. :
_bill. ;
_c30 cm. +
_e1 CD-ROM
502 _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2013
504 _aBibliography : p. 39-41
520 3 _aPropane dehydrogenation is a one of a promising route for producing propylene by using thermodynamic analysis to replace traditional cracking methods. The purpose of this study is to product distribution as a function over temperature, to identifying the region of the carbon deposition and to analysis the effect of temperature on the equilibrium constant. Hydrogen production varies significantly according to the operating conditions such as pressure, temperature and feed reactants ratio. The thermodynamic analysis provides important knowledge about the effects of those variables on the process of propane dehydrogenation. The present work was aimed at analyzing the thermodynamic propane dehydrogenation of propylene, using Gibbs free energy minimization with actual temperature and pressure data found in the literature. The results showed that the extent of side reactions strongly depends on the operating conditions. By computing carbon activities in experimental systems, it was also possible to explain deviations between thermodynamic analysis and experimental results regarding carbon deposition. From the results obtained¸ all of possible reactions are endothermic reaction and the dehydrogenation temperature needs to be evaluated to beyond 500 K to 600 K.
650 0 _aThermodynamics
650 0 _aDehydrogenation
650 0 _aPropylene carbonate
999 _aVIRTUA40
_c4240
_d4246
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*6501*6502*9992