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13篇 您的检索式：作者名="Chang Pengmei"

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		题名	作者	年代	出处	被引量
	1	Novel catalyst for cracking of biomass tar 显示文摘	Wang Tiejun Chang Jie Lv Pengmei	2005	Energy & Fuels2005，19，：	1
	2	Novel catalyst for cracking of biomass tar显示文摘	Wang Tiejun Chang Jie Lv Pengmei	2005	Energy & Fuels2005，19，：	1
	3	Biomass airsteam gasification in a fluidized bed to produce hydrogen-rich gas显示文摘	Lv Pengmei Chang Jie Xiong Zuhong	2003	Energy and Fuels2003，17，：	1
	4	Hydrogen-rich gas production from biomass catalytic gasification显示文摘	Lv Pengmei Chang Jei Wang Tiejun	2004	Energy and Fuels2004，18，：	1
	5	Crystal morphology control of AlPO4-11 molecular sieves by microwave irradiation 显示文摘	Chen Yashao Luo Xiaolin Chang Pengmei	2009	Materiials Chemis- try and Physics2009，113，：	1
	6	Biomass air-steam gasification in a fluidized bed to produce hydrogen-rich gas 显示文摘	PENGMEI LV JIE CHANG ZUHONG XIONG et d	2003	Energy & Fuels2003，17，3：	1
	7	A kinetic study on biomass fast catalytic pyrolysis显示文摘	Lv Pengmei Chang Jie Wang Tiejun	2004	Energy and Fuels2004，18，6：	1
	8	An experimental re- search on biomass air-steam gasification in a fluidized bed 显示文摘	Lv Pengmei Chang Jie Xiong Zhuhong	2004	Bioresource Technology2004，95，1：	1
	9	Biomass air- steam gasification in a fluidized bed to produce hydrogen-rich gas显示文摘	Lv Pengmei Xiong Z H Chang J	2003	Energy & Fuels2003，17，3：	1
	10	Biomass airsteam gasification in a fluidized bed to produce hydrogenrich gas显示文摘	Lv Pengmei Jie Chang Xing Zuhong	2003	Energy & Fuel2003，17，3：	1
	11	Crystal Morphology Control of A1PO4-11 Molecular Sieves by Micro- wave Irradiation显示文摘	Chen Yashao Luo Xiaolin Chang Pengmei	2009	Mater Chem Phys2009，113，8：	1
	12	Novel Catalyst for Cracking of Biomass Tar显示文摘	Wang Tiejun Chang Jie Lv Pengmei	2005	Energy & Fuels2005，19，1：	1
	13	Modeling and simulation of biomass air-steam gasification in a fluidized bed显示文摘By considering the features of fluidized-bed reactors and the kinetic mechanism of biomass gasification,a steady-state,isothermal,one-dimensional and twophase mathematical model of biomass gasification kinetics in bubbling fluidized beds was developed.The model assumes the existence of two phases–a bubble and an emulsion phase–with chemical reactions occurring in both phases.The axial gas dispersion in the two phases is accounted for and the pyrolysis of biomass is taken to be instantaneous.The char and gas species CO,CO_(2),H_(2),H_(2)O,CH_(4) and 8 chemical reactions are included in the model.The mathematical model belongs to a typical boundary value problem of ordinary differential equations and its solution is obtained by a Matlab program.Utilizing wood powder as the feedstock,the calculated data show satisfactory agreement with experimental results and proves the effectiveness and reliability of the model.	Pengmei Lü Xiaoying KONG Chuangzhi WU Zhenhong YUAN Longlong MA Jie CHANG	2008	Frontiers of Chemical Science and Engineering2008，2，2：	0

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