How to Avoid Bed Agglomeration in the Bubbling Fluidized Bed Biomass Gasification: Two-Stage Gasification at 600 °C

2021 ◽  
Author(s):  
Jong-Woo Kim ◽  
Yong-Seong Jeong ◽  
Joo-Sik Kim
Keyword(s):  
Fluidized Bed ◽  
Biomass Gasification ◽  
Two Stage ◽  
Bubbling Fluidized Bed ◽  
Bed Agglomeration

Simulation of biomass gasification in bubbling fluidized bed reactor using aspen plus®

2021 ◽  
Vol 235 ◽  
pp. 113981
Author(s):  
M. Puig-Gamero ◽  
D.T. Pio ◽  
L.A.C. Tarelho ◽  
P. Sánchez ◽  
L. Sanchez-Silva
Keyword(s):  
Fluidized Bed ◽  
Aspen Plus ◽  
Fluidized Bed Reactor ◽  
Biomass Gasification ◽  
Bubbling Fluidized Bed

Particle behaviours of biomass gasification in a bubbling fluidized bed

2021 ◽  
pp. 131847
Author(s):  
Dali Kong ◽  
Kun Luo ◽  
Shuai Wang ◽  
Jiahui Yu ◽  
Jianren Fan
Keyword(s):  
Fluidized Bed ◽  
Biomass Gasification ◽  
Bubbling Fluidized Bed

Biomass Gasification in a Bubbling Fluidized Bed Reactor

2020 ◽  
Vol 6 (2) ◽  
Author(s):  
D.V. Baratha Dodawatta ◽  
U.D. Indula ◽  
N.A.C.J.D. Senarathna ◽  
D.G.C. Wickramasinghe ◽  
M. Narayana
Keyword(s):  
Fluidized Bed ◽  
Fluidized Bed Reactor ◽  
Biomass Gasification ◽  
Bubbling Fluidized Bed

Investigation of Ash-Related Issues During Combustion of Maize Straw and Wood Biomass Blends in Lab-Scale Bubbling Fluidized Bed Reactor

2019 ◽  
Vol 142 (2) ◽  
Author(s):  
Krzysztof Głód ◽  
Janusz Lasek ◽  
Krzysztof Słowik ◽  
Jarosław Zuwała ◽  
Daniel Nabagło ◽  
...  
Keyword(s):  
Fluidized Bed ◽  
Air Velocity ◽  
Interesting Phenomenon ◽  
Simultaneous Application ◽  
Agglomeration Process ◽  
Bubbling Fluidized Bed ◽  
Bed Agglomeration ◽  
The Cost ◽  
The Impact ◽  
Combustion Of Solid Fuels

Abstract During the combustion of solid fuels, the undesired effects of ash transformation include bed agglomeration, slagging, and fouling processes. In particular, a problematic consequence of bed agglomeration is the defluidization process, resulting from the disappearance of gaseous bubbles that are created behind air distributors. Different solutions can be applied against the agglomeration process. One possible method is to apply some additives that influence the ash behavior, thus inhibiting the agglomeration process. This paper presents the results of investigations into ash-related issues in a laboratory-scale bubbling fluidized bed (BFB) reactor. In particular, the impact of additives (kaolin, halloysite, fly ash, and the residuals from wet desulfurization system (IMOS)) on bed agglomeration was investigated. It was found that the addition of these compounds increased the defluidization time from ∼109 min (without additive) to ∼285 min in the BFB (with the addition of 0.1 g/min of kaolin). The morphology of additive (kaolin and halloysite) transformation after their addition into the combustion chamber was discussed. Another interesting phenomenon is that residuals from the IMOS exhibited the ability to be an additive against the agglomeration process. The defluidization time can be also significantly increased by the simultaneous application of the additive and the control of fluidization air velocity. The procedure of periodical bed moving by impulse primary air feeding against defluidization (PADM) is suggested and discussed. The PADM procedure resulted in a 36% reduction of additive, thus reducing the cost of measures against ash-related issues.

Particle-scale modeling of biomass gasification in the three-dimensional bubbling fluidized bed

2019 ◽  
Vol 196 ◽  
pp. 1-17 ◽  
Author(s):  
Shiliang Yang ◽  
Hua Wang ◽  
Yonggang Wei ◽  
Jianhang Hu ◽  
Jia Wei Chew
Keyword(s):  
Fluidized Bed ◽  
Three Dimensional ◽  
Biomass Gasification ◽  
Scale Modeling ◽  
Bubbling Fluidized Bed
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