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12篇 您的检索式：作者名="Formisani"

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		题名	作者	年代	出处	被引量
	1	Packing and fluidization Prosperities of binary mixtures of spherical Particles显示文摘	Formisani B	1991	Powder Technology1991，66，：	1
	2	The fludization process of binary mixtures of solids: development of the approach based on thefluidization velocity interval 显示文摘	Formisani R Girimonte R Longo T	2008	Powder Technology2008，185，2：	1
	3	The minimum bubbling velocity of fluidized beds operating at high temperature显示文摘	Girimonte R Formisani B	2009	Powder Technology2009，189，1：	1
	4	A fundamental approach to the phenomenology of fluidization of size segregating binary mixtures of solids 显示文摘	Formisani B Cristofaro G D Girimonte R	2001	Chemical Engineering Science2001，56，1：	1
	5	The influence of temperature on the properties of the particulate phase at incipient fluidization 显示文摘	Raso G D' Amore M Formisani B	1992	Powder Technology1992，72，：	1
	6	Analysis of the fluidization process of particle beds at high temperature显示文摘	Formisani B Girimonte R Mancuso L	1998	Chemical Engineering Science1998，53，：	1
	7	Fundamental approach to the phenomenology of fluidization of size segregating binary mixtures of solids 显示文摘	Formisani B De Cristofaro C Girimonte R A	2001	Chem Eng Sei2001，6，1：	1
	8	The Fluidization Process of Binary Mixtures of Solids: Development of the Approach Based on the Fluidization Velocity Interval 显示文摘	Formisani B Girimonte R and Longo T	2008	Powder Technol2008，185，2：	1
	9	A fundamental approach to the phenomenology of fluidization of size segregating binary mixtures of solids显示文摘	Formisani B De Cristofaro G Girimonte R	2001	Chemical Engineering Science2001，56，：	1
	10	查看详情显示文摘	Renzo A B Maio F P Girimonte R Formisani B		0，，：	1
	11	The fluidization process of binary mixtures of solids:development of the approach based on the fluidization velocity interval 显示文摘	Formisani B Girimonte R Longo T	2008	Powder Technology2008，185，2：	1
	12	CO2 adsorption in a confined fluidized bed of zeolite pellets: Influence of operating velocity显示文摘CO2 adsorption is performed across a fluidized bed comprising a commercial pelletized 13X zeolite con-fined to the interstitial void network of a coarse glass sphere packed bed. Compared with traditional fixed bed adsorption, the packed fluidized system allows operation across a wide-range of gas velocities without a substantial increase in pressure drop. Additionally, with respect to conventional fluidization regimes, the technique adopted herein prevents the formation of bubbles in favour of enhancing the bed expansion ability. Furthermore, for a given mass of sorbent, the C02 uptake capacity is observed to increase as a result of improved thermal conditions and in eliminating any by-pass effect at the gas-particle interface, which is associated to the suppression of bubbling.	Rossella Girimonte Brunello Formisani Flaviano Testa	2019	Particuology2019，17，5：	0

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