000			01534nab a2200205 4500
005			20260520000837.0
008			260224s2009 xxu
245	0	0	_aPyrolysis performances of catalytic cracking naphtha and coker naphtha on inert carriers and an active catalyst
260			_a _b _cnov./dic. 2009
270			_a09/06/2010 ; 09/06/2010
300			_a5 p. ; 5760-5764
520			_aTranscripción del resumen del autor. The pyrolysis performance of catalytic cracking naphtha and coker naphtha on different carriers and an active catalyst was investigated in a confined fluidized bed reactor. For the pyrolysis of catalytic cracking naphtha on quartz grain, the yield of total light olefins increased with the enhancement of temperature, while it varied slightly with increasing weight hourly space velocity (WHSV) and steam/oil weight ratio. The optimal reaction temperature, WHSV, and steam/oil weight ratio were 700 °C, 5.7 h-1, and 0.5, respectively. The selectivity of total light olefins of coker naphtha was better than that of catalytic cracking naphtha under the optimal reaction conditions. The surface area and pore size of the inert carrier showed little effect on the pyrolysis performance. The introduction of the active catalyst could improve the conversion and the yield of total light olefins.
581			_a6
773	0		_tEnergy & fuels _g23
942			_cARTICULO
100	1		_aLiu, Weikang _942339
100	1		_aMeng, Xianghai _940827
100	1		_aZhao, Xu _942340
999			_c170815 _d170815