2020
DOI: 10.1016/j.enconman.2020.113116
|View full text |Cite
|
Sign up to set email alerts
|

Experimental investigation of syngas composition variation along updraft fixed bed gasifier

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
24
0

Year Published

2021
2021
2024
2024

Publication Types

Select...
8
1
1

Relationship

0
10

Authors

Journals

citations
Cited by 75 publications
(24 citation statements)
references
References 39 publications
0
24
0
Order By: Relevance
“…Due to the gas cooling when it is drifted upwards, some of the tar is condensed on the falling biomass while large amounts leave the gasifier with the producer gas. Thus, this type of gasifiers suffers from its high tar content that typically exceeds 100 g/Nm 3 which limits its usage for thermal applications rather than power production [59]. The producer gas is cooled down to approximately 200°C while passing through the drying zone, leading to significant enhancement in cold gas efficiency in comparison to other types of fixed-bed gasifiers [60]).…”
Section: Updraft Gasifiermentioning
confidence: 99%
“…Due to the gas cooling when it is drifted upwards, some of the tar is condensed on the falling biomass while large amounts leave the gasifier with the producer gas. Thus, this type of gasifiers suffers from its high tar content that typically exceeds 100 g/Nm 3 which limits its usage for thermal applications rather than power production [59]. The producer gas is cooled down to approximately 200°C while passing through the drying zone, leading to significant enhancement in cold gas efficiency in comparison to other types of fixed-bed gasifiers [60]).…”
Section: Updraft Gasifiermentioning
confidence: 99%
“…Tar formation is one of the major technical challenges of updraft gasification. Cerone et al found that the type of gasifying agent residence time and average reaction temperature affected the tar yield [56]. Specifically, the tar yield was 137 g/kg in air gasification and 163 g/kg in the air/steam gasification.…”
Section: Types Of Gasification Reactorsmentioning
confidence: 99%
“…In the case of the reactor design, several studies analyzed how is the behavior of the BFB gasification process is and how the reactor design is affected by bed material [15][16][17], bed agglomeration [18][19][20][21][22], gasifying agent [9,10,[23][24][25][26], use of catalysts [20,27,28], hydrodynamics [2,29], biomass segregation [5,30], kind and size of biomass [25,[30][31][32][33][34][35], temperature conditions [32,36], or gasification process [37][38][39]. Results from the experimental test were also studied in [23,24,33,34,[40][41][42], and finally, other publications integrated models and tests to validate simulations [43,44]. In addition, some reviews compared researcher works carried out in the biomass gasification field [31,[45][46][47]…”
Section: Introductionmentioning
confidence: 99%