000			01980ntm a2200241 a 4500
001			vtls000074669
003			KUKTEM
005			20251114204542.0
008			130924t2013 my da f m 000 0 eng d
020			_aTHE0004774(Local)
039		9	_a201905151116 _bsmfh _c201309261136 _dhuda _y201309241311 _zhuda
040			_aUMP
090			_aTP492.5 .K66 2013 rs Bc.
100	1		_aKong Zi, Ying
245	1	0	_aThermodynamic analysis of methane dry reforming / _cKong Zi Ying
260			_aKuantan, Pahang : _bUMP, _c2013
300			_axii, 43 p. : _bill. (some col.) ; _c30 cm. + _e1 CD-ROM
502			_aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2013
504			_aBibliography : p. 33-34
520	3		_aIt is well known that methane (a natural gas that is abundantly available) can be reacted with carbon dioxide to produce synthesis gas (a mixture of hydrogen gas and carbon monoxide). Syngas may be converted to gasoline-grade fuels via Fischer-Tropsch synthesis since the petrochemicals in the world was becoming lesser and lesser. In lieu of the significance of the said reaction, the objective for the current work is to study the thermodynamic aspect of methane dry reforming at reforming temperature from 500 to 1000K at atmospheric pressure and different methane to carbon dioxide ratios. The method used in this research is Gibbs free energy minimization. Computation results showed that the temperature affected the product distribution. At low temperature (500K), thermodynamic consideration alone indicated that the methane dry reforming reaction is almost non-existent. Different CO2/CH4 ratios decrease the temperature at which the onset of carbon deposition occurs. Carbon forms at lower temperature and high reactant ratio. At temperature 1000K and CO2:CH4 ratio of 3, the carbon formation value is 1.7.
650		0	_aThermodynamics
999			_aVIRTUA40 _c3989 _d3995
999			_aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*9992