[1]Yuranov I,Kiwi M L,Renken A.Sturetured combustion catalysts based on sintered metal fibre filters[J].Applied Catalysis,2003,43:217227.
[2]Roy S,Heibel A K,Liu W,et al.Design of monolithic catalysts for multiphase reactions[J].Chemical Engineering Science,2004,59(5):957966.
[3]李霄宇.低浓度甲烷催化燃烧整体式催化剂的研究[D].北京:北京化工大学化工学院,2008.
[4]Thomas H,Elmer. Ultralow thermal expansion ceramics articles:US,3958058[P].1976-5-18.
[5]Shiga Pov A N,Graham G W,Maeeabe R W,et al.The PreParation of high Surface are cordierite monolith hyaeid treatment[J].Applied Catalysis A:General,1999,182(1):137146.
[6]白佳海,郭露村.酸处理对革青石质蜂窝陶瓷性能的影响[J].中国陶瓷工业,2005,12(1):14.
[7]华金铭,郑 起,魏可镁,等.酸蚀预处理对蜂窝状荃青石及其不同方法涂敷氧化铝涂层的影响[J].分子催化,2006,20(6):550555.
[8]田建民,白雪,李健,等.载体预处理对CuOCeO菁青石催化剂性能的影响[J].内蒙古工业大学学报,2006,25(3):210214.
[9]贺振富,邵 潜,沈宁元.载体预处理对催化剂涂层结构的影响[J].石油学报,2001,17(3):8385.
[10]Beauseigneur P A,Lachman I M,Patil M D.Pore impregnated catalyst device:US,5334570[P].1994-8-2.
[11]Duisterwinkel A E.Clean coal combustion with in situ impregnated sol-gel sorbent[D].Delft:Faculty of Applied Science,Delft University of Technology,1991.
[12]Addiego W P,Lachman I M,Patil M D,et al.High surface area washcoated substrate and method for producing same:US,5212130[P].1993-5-18.
[13]安琴,冯长根,曾庆轩,等.陶瓷蜂窝载体γAl2O3涂层研究进展[J].化学通报,2001(3):130140.
[14]史惠萍.蜂窝陶瓷催化剂的开发及其应用[J].江苏陶瓷,1997(2):1214.
[15]王大祥,王丽琼,安琴,等.故障树分析法(FTA)在制备γAl2O3涂层中的应用[J].上海化工,2002,6:1215.
[16]王伟,刘玺,张浩,等.堇青石质蜂窝陶瓷载体的表面改性[J].应用科技,2007,34(3):6972.
[17]Jiang Ping Ping,Lua Guan Zhong,Guo Yun,et al.Preparation and properties of a γAl2O3 washcoat deposited on a ceramic honeycomb[J].Surface & Coatings Technology,2004,190:314320.
[18]黄莹.金属载体的活性氧化铝涂层工艺研究[D].天津:天津大学化工学院,2005.
[19]Nijhuis T A,Kreutzer M T,Romijn A C,et al.Monolithic catalysts as more efficient threephase reactors[J].Catalysis Today,2001,66(24):157165.
[20]Agustin F,Perez Cadenas,Freek Kapteijn,et al.Tuning the morphology of monolith coatings[J].Applied Catalysis A,2007,319:267271.
[21]田久英,卢菊生,吴宏.堇青石蜂窝陶瓷载体涂层的制备研究[J].徐州师范大学学报:自然科学版,2008,26(4):6871.
[22]郝树甫,董国君,龚凡,等.改性堇青石载体催化剂选择性催化还原NOx研究[J].应用化工,2008,37(2):153157.
[23]董国君,常雪,王桂香,等.CuO/SiO2Al2O3/堇青石催化剂选择性还原NOx性能研究[J].应用化工,2009,38(5):654658.
[24]Agrafiotis G,Tsetsekou A.The effect of powder characteristics on washcoat quality.Part I:Alumina washcoats[J].Journal of the European Ceramic Society,2000,20:815824.
[25]蒋平平,张顺海,郭杨龙,等.三效催化剂涂层制备与性能研究[J].无机材料学报,2004,19(3):634640.
[26]王春永.堇青石、氧化铝为载体的负载型把催化剂对丙酮催化氧化反应性能的研究[D].杭州:浙江大学环境与资源学院,2006.
[27]沈美庆,王 军,翁 端,等.堇青石蜂窝陶瓷载体涂层与热稳定性研究[J].中国稀土学报,2003,21:3134.
[28]王家祥,王继先,王大祥.BaO热稳定γAl2O3蜂窝陶瓷涂层的试验研究[J].安徽农业大学学报,2005,32(1):9194.
[29]Nakatsuji T,Okuno M,Yashimoto M.Catalysis for removal of nitrogen oxide,hydrocarbons,and carbon monoxide from waste gases:JP,0576762[P].1993-3-30.
[30]Kikuchi R,Maeda S,Sasaki K,et al.Catalytic activity of oxidesupported Pd catalysts on a honeycomb for lowtemperature methane oxidation[J].Applied Catalysis,2003,239:169179.
[31]Hart M H,Aim Y S,Kim S K,et a1.Synthesis of manganese sultituted hexaalnminate and its fabrication into monolithic honeycombs for catalytic combustion[J].Mater Science Engineering A,2001,302:286293.
[32]华金铭,郑起,林性贻,等.整体式高温水煤气变换催化剂的初步研制[J].工业催化,2003,11(3):1620.
[33]Edvinsson A R,Nystromm M,Siverstrom M,et al.Development of a monolithic based process for H2O2 production:from Idea to LargeScale Implementation[J].Catalysis Today,2001,69(3):247252.
[34]Groppi G,Tronconi E.Simulation of structure catalytic reactor with enhanced thermal conductivity for selective oxidation reaction[J].Catalysis Today,2001, 69(1):6373.
[1]张芳,黄志良.利用不同成孔剂制备堇青石质多孔陶瓷[J].武汉工程大学学报,2008,(03):69.
ZHANG Fang,HUANG Zhi liang.Comparison of cordierite porous ceramics made from different poreforming materials[J].Journal of Wuhan Institute of Technology,2008,(07):69.
[2]周爱军,卢琪,万香港,等.溶胶\|凝胶过程影响堇青石结晶行为的因素[J].武汉工程大学学报,2012,(06):13.[doi:103969/jissn16742869201206004]
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