A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser

Chao Zhu; Jun You

A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser

Mechanical and Industrial Engr

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution

Abstract

Circulating fluidized beds (CFB) find a wide-spread application in a variety of industrial processes such as coal combustion and coal gasification, catalytic cracking of oil, and gas purification. A one-dimensional model is developed to characterize the pressure drop partitions among solids concentration, solids acceleration, and energy loss in the acceleration zone in a CFB riser. The axial distributions of solid velocity and solid concentration are obtained by solving the equations. Consequently effects of solids acceleration and energy loss on the axial distributions of solids velocity and concentration are presented. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).

Original language	English (US)
Title of host publication	05AIChE
Subtitle of host publication	2005 AIChE Annual Meeting and Fall Showcase, Conference Proceedings
Publisher	American Institute of Chemical Engineers
ISBN (Print)	0816909962, 9780816909964
State	Published - 2005
Event	05AIChE: 2005 AIChE Annual Meeting and Fall Showcase - Cincinnati, OH, United States Duration: Oct 30 2005 → Nov 4 2005

Publication series

Name	AIChE Annual Meeting Conference Proceedings
Volume	2005

Other

Other	05AIChE: 2005 AIChE Annual Meeting and Fall Showcase
Country/Territory	United States
City	Cincinnati, OH
Period	10/30/05 → 11/4/05

All Science Journal Classification (ASJC) codes

General Energy

Cite this

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title = "A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser",

abstract = "Circulating fluidized beds (CFB) find a wide-spread application in a variety of industrial processes such as coal combustion and coal gasification, catalytic cracking of oil, and gas purification. A one-dimensional model is developed to characterize the pressure drop partitions among solids concentration, solids acceleration, and energy loss in the acceleration zone in a CFB riser. The axial distributions of solid velocity and solid concentration are obtained by solving the equations. Consequently effects of solids acceleration and energy loss on the axial distributions of solids velocity and concentration are presented. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).",

author = "Chao Zhu and Jun You",

year = "2005",

language = "English (US)",

isbn = "0816909962",

series = "AIChE Annual Meeting Conference Proceedings",

publisher = "American Institute of Chemical Engineers",

booktitle = "05AIChE",

address = "United States",

note = "05AIChE: 2005 AIChE Annual Meeting and Fall Showcase ; Conference date: 30-10-2005 Through 04-11-2005",

}

Zhu, C & You, J 2005, A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser. in 05AIChE: 2005 AIChE Annual Meeting and Fall Showcase, Conference Proceedings. AIChE Annual Meeting Conference Proceedings, vol. 2005, American Institute of Chemical Engineers, 05AIChE: 2005 AIChE Annual Meeting and Fall Showcase, Cincinnati, OH, United States, 10/30/05.

A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser. / Zhu, Chao; You, Jun.
05AIChE: 2005 AIChE Annual Meeting and Fall Showcase, Conference Proceedings. American Institute of Chemical Engineers, 2005. (AIChE Annual Meeting Conference Proceedings; Vol. 2005).

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution

TY - GEN

T1 - A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser

AU - Zhu, Chao

AU - You, Jun

PY - 2005

Y1 - 2005

N2 - Circulating fluidized beds (CFB) find a wide-spread application in a variety of industrial processes such as coal combustion and coal gasification, catalytic cracking of oil, and gas purification. A one-dimensional model is developed to characterize the pressure drop partitions among solids concentration, solids acceleration, and energy loss in the acceleration zone in a CFB riser. The axial distributions of solid velocity and solid concentration are obtained by solving the equations. Consequently effects of solids acceleration and energy loss on the axial distributions of solids velocity and concentration are presented. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).

AB - Circulating fluidized beds (CFB) find a wide-spread application in a variety of industrial processes such as coal combustion and coal gasification, catalytic cracking of oil, and gas purification. A one-dimensional model is developed to characterize the pressure drop partitions among solids concentration, solids acceleration, and energy loss in the acceleration zone in a CFB riser. The axial distributions of solid velocity and solid concentration are obtained by solving the equations. Consequently effects of solids acceleration and energy loss on the axial distributions of solids velocity and concentration are presented. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).

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M3 - Conference contribution

AN - SCOPUS:33646721988

SN - 0816909962

SN - 9780816909964

T3 - AIChE Annual Meeting Conference Proceedings

BT - 05AIChE

PB - American Institute of Chemical Engineers

T2 - 05AIChE: 2005 AIChE Annual Meeting and Fall Showcase

Y2 - 30 October 2005 through 4 November 2005

ER -

A one-dimensional model of gas-solids flows in the acceleration zone of a CFB riser

Abstract

Publication series

Other

All Science Journal Classification (ASJC) codes

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