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第6期 徐立昊等:入口气组分对质子交换膜燃料电池柴油水蒸气重整制氢流程的影响 ·717· [5]Dae HK,Jung S K,Yun JL,et al.Steam reforming of n-hexade- improving catalyst stability over Pt/ceria during ethanol steam re- cane over noble metal-modified Ni-based catalysts.Catal Today, forming:Sn addition and CO,co-feeding.Appl Catal B,2010, 2008,136(314):228 96(3/4):387 6]Sehested J,Gelten J A P,Remediakis I N,et al.Sintering of [20]Arena F,Trunfio G,Alongi E,et al.Modelling the activity-sta- nickel steam-reforming catalysts:effects of temperature and steam bility pattem of Ni/Mgo catalysts in the pre-reforming of n-hex- and hydrogen pressures.J Catal,2004,223(2):432 ane.Appl Catal A,2004,266(2):155 Pema A.Hydrogen from ethanol:theoretical optimization of a 1]Gong J,Su QQ.Mi W L,et al.Effect of inlet gas composition PEMFC system integrated with a steam reforming processor.IntJ on working temperature of natural gas steam reforming.J Chem Hydrogen Energy,2007,32(12):1811 Ind Eng China,2008,59 (3):687 [8]Alvarez-Galvan M C,Navarro R M,Rosa F,et al.Performance of (龚娟,苏庆泉,米万良,等.入口气体组成对天然气重整工 La,Ce-modified alumina-supported P and Ni catalysts for the ox 作温度的影响.化工学报,2008,59(3):687) dative reforming of diesel hydrocarbons.Int J Hydrogen Energy, [2]Mi W L,Sun D J,Gong J,et al.CO water-gas-shift reaction 2008,33(2):652 character over Cu-Zn catalyst.J Unir Sci Technol Beijing,2010, 9]Parmar R D,Kundu A,Karan K.Thermodynamic analysis of 32(2):224 diesel reforming process:mapping of carbon formation boundary (米万良,孙丹杰,龚娟,等.Cu一Zm催化剂的C0水汽变换反 and representative independent reactions.Power Sources,2009, 应特性.北京科技大学学报,2010,32(2):224) 194(2):1007 [23]Li Z Y,Mi W L,Gong J,et al.CO removal by two-stage metha- [10]Sharma S,Deshpande P A,Hedge M S,et al Nondeactivating nation for polymer electrolyte fuel cell.J Nat Gas Chem,2008, nanosized ionic catalysts for water-gas shift reaction.Ind Eng 17(4):359 Chem Res,2009,48(14):6535 24 Hernandez L,Kafarov V.Thermodynamic evaluation of hydrogen [11]Choudhury M B I,Ahmed S,Shalabi M A,et al.Preferential production for fuel cells by using bio-ethanol steam reforming: methanation of CO in a syngas involving CO2 at lower temperature effect of carrier gas addition.J Power Sources,2009,192 (1): range.Appl Catal A,2006,314(1)47 195 [12]Xu L H.Mi W L,Su QQ.Hydrogen production through diesel D5]Batista M S,Santiago E I,Assaf E M,et al.Evaluation of the steam reforming over rare-earth promoted Ni/y-l2O:catalysts. water-gas shift and CO methanation processes for purification of Nat Gas Chem,2011,20(3):287 reformate gases and the coupling to a PEM fuel cell system. 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Steam reforming of n-hexade￾cane over noble metal-modified Ni-based catalysts. Catal Today, 2008,136( 3 /4) : 228 [6] Sehested J,Gelten J A P,Remediakis I N,et al. Sintering of nickel steam-reforming catalysts: effects of temperature and steam and hydrogen pressures. J Catal,2004,223( 2) : 432 [7] Perna A. Hydrogen from ethanol: theoretical optimization of a PEMFC system integrated with a steam reforming processor. Int J Hydrogen Energy,2007,32( 12) : 1811 [8] Alvarez-Galvan M C,Navarro R M,Rosa F,et al. Performance of La,Ce-modified alumina-supported Pt and Ni catalysts for the oxi￾dative reforming of diesel hydrocarbons. Int J Hydrogen Energy, 2008,33( 2) : 652 [9] Parmar R D,Kundu A,Karan K. Thermodynamic analysis of diesel reforming process: mapping of carbon formation boundary and representative independent reactions. J Power Sources,2009, 194( 2) : 1007 [10] Sharma S,Deshpande P A,Hedge M S,et al Nondeactivating nanosized ionic catalysts for water-gas shift reaction. Ind Eng Chem Res,2009,48( 14) : 6535 [11] Choudhury M B I,Ahmed S,Shalabi M A,et al. Preferential methanation of CO in a syngas involving CO2 at lower temperature range. Appl Catal A,2006,314( 1) : 47 [12] Xu L H,Mi W L,Su Q Q. Hydrogen production through diesel steam reforming over rare-earth promoted Ni /γ-Al2O3 catalysts. J Nat Gas Chem,2011,20( 3) : 287 [13] Christensen T S. Adiabatic prereforming of hydrocarbons: an im￾portant step in syngas production. Appl Catal A,1996,138( 2) : 285 [14] Cromarty B J,Hooper C W. Increasing the throughput of an ex￾isting hydrogen plant. Int J Hydrogen Energy,1997,22( 1) : 17 [15] Armor J N. The multiple roles for catalysis in the production of H2 . Appl Catal A,1999,176( 2) : 159 [16] Peters R,Riensche E,Cremer P. Pre-reforming of natural gas in solid oxide fuel-cell systems. J Power Sources,2000,86( 1 /2) : 432 [17] Laosiripojana N,Assabumrungrat S. Catalytic steam reforming of ethanol over high surface area CeO2 : the role of CeO2 as an inter￾nal pre-reforming catalyst. Appl Catal B,2006,16( 1 /2) : 29 [18] Chen F Z,Zha S W,Dong J,et al. Pre-reforming of propane for low-temperature SOFCs. Solid State Ionics,2004,166 ( 3 /4 ) : 269 [19] de Lima S M,da Silva A M,Jacobs G,et al. New approaches to improving catalyst stability over Pt /ceria during ethanol steam re￾forming: Sn addition and CO2 co-feeding. Appl Catal B,2010, 96( 3 /4) : 387 [20] Arena F,Trunfio G,Alongi E,et al. Modelling the activity-sta￾bility pattern of Ni /MgO catalysts in the pre-reforming of n-hex￾ane. Appl Catal A,2004,266( 2) : 155 [21] Gong J,Su Q Q,Mi W L,et al. Effect of inlet gas composition on working temperature of natural gas steam reforming. J Chem Ind Eng China,2008,59( 3) : 687 ( 龚娟,苏庆泉,米万良,等. 入口气体组成对天然气重整工 作温度的影响. 化工学报,2008,59( 3) : 687) [22] Mi W L,Sun D J,Gong J,et al. CO water-gas-shift reaction character over Cu-Zn catalyst. J Univ Sci Technol Beijing,2010, 32( 2) : 224 ( 米万良,孙丹杰,龚娟,等. Cu--Zn 催化剂的 CO 水汽变换反 应特性. 北京科技大学学报,2010,32( 2) : 224) [23] Li Z Y,Mi W L,Gong J,et al. CO removal by two-stage metha￾nation for polymer electrolyte fuel cell. J Nat Gas Chem,2008, 17( 4) : 359 [24] Hernndez L,Kafarov V. Thermodynamic evaluation of hydrogen production for fuel cells by using bio-ethanol steam reforming: effect of carrier gas addition. J Power Sources,2009,192( 1) : 195 [25] Batista M S,Santiago E I,Assaf E M,et al. Evaluation of the water-gas shift and CO methanation processes for purification of reformate gases and the coupling to a PEM fuel cell system. J Power Sources,2005,145( 1) : 50 [26] Laosiripojana N,Sutthisripok W,Charojrochkul S,et al. Steam reforming of LPG over Ni and Rh supported on Gd-CeO2 and Al2O3 : effect of support and feed composition. Fuel,2011,90 ( 1) : 136 [27] Xie C,Chen Y S,Li Y,et al. Influence of sulfur on the carbon deposition in steam reforming of liquid hydrocarbons over CeO2 - Al2O3 supported Ni and Rh catalysts. Appl Catal A,2011,394 ( 1 /2) : 32 [28] Zheng J,Strohm J J,Song C S. Steam reforming of liquid hydro￾carbon fuels for micro-fuel cells: pre-reforming of model jet fuels over supported metal catalysts. Fuel Process Technol,2008,89 ( 4) : 440 [29] Li Z Y,Mi W L,Su Q Q. Deep removal of CO in reformate. J Univ Sci Technol Beijing,2010,32( 1) : 100 ( 李志远,米万良,苏庆泉. 重整气中 CO 深度去除方法. 北 京科技大学学报,2010,32( 1) : 100) ·717·
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