1993
DOI: 10.1016/0360-1285(93)90003-w
|View full text |Cite
|
Sign up to set email alerts
|

Combustion and gasification of coals in fixed-beds

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2
1

Citation Types

4
92
0
6

Year Published

2001
2001
2021
2021

Publication Types

Select...
7
2

Relationship

0
9

Authors

Journals

citations
Cited by 173 publications
(102 citation statements)
references
References 134 publications
4
92
0
6
Order By: Relevance
“…Therefore, the produced gas is cleaner than the equivalent provided by the countercurrent model. The co-current version presents some limitations on controllability for large diameters or power output [9,10].This is mostly due to the formation of preferential channels in the fuel bed that prevent the tar rich stream moving from the pyrolysis region from meeting the hot core of the combustion region. Nevertheless, that problem is mitigated through the application of slow-rotating paddles to provide uniform distribution of particles in the bed [11].…”
Section: A Downdraft Gasificationmentioning
confidence: 99%
“…Therefore, the produced gas is cleaner than the equivalent provided by the countercurrent model. The co-current version presents some limitations on controllability for large diameters or power output [9,10].This is mostly due to the formation of preferential channels in the fuel bed that prevent the tar rich stream moving from the pyrolysis region from meeting the hot core of the combustion region. Nevertheless, that problem is mitigated through the application of slow-rotating paddles to provide uniform distribution of particles in the bed [11].…”
Section: A Downdraft Gasificationmentioning
confidence: 99%
“…The moisture evaporation should be considered in two ways: boiling and diffusion below the boiling temperature. The reaction rate of char combustion is determined from the kinetic rate, diffusion rate and internal mass transport in the ash layer of the particle (8) . It can be expressed as Eq.…”
Section: Numerical Approachmentioning
confidence: 99%
“…From this factor and the combustion rate, the particle size and the internal porosity are determined. The changes in the particle size are described by well-known models: the shell progressive (SP) and ash segregation (AS) models (8) .…”
Section: Numerical Approachmentioning
confidence: 99%
“…The novel Lurgi fixed-bed gasifiers suffer from high tar yields in the product gases (Li X.T. et al, 2004), and the processing rates are slow compared with entrained-and fluidized-beds (Hobbs et al, 1993). Fluidized beds now find wide application in coal gasification (Li X.T.…”
Section: Introductionmentioning
confidence: 99%