2017
DOI: 10.1016/j.wasman.2017.08.006
|View full text |Cite
|
Sign up to set email alerts
|

Refuse Derived Fuel (RDF) production and gasification in a pilot plant integrated with an Otto cycle ICE through Aspen plus™ modelling: Thermodynamic and economic viability

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

8
22
0
6

Year Published

2018
2018
2024
2024

Publication Types

Select...
5
4

Relationship

0
9

Authors

Journals

citations
Cited by 101 publications
(44 citation statements)
references
References 41 publications
8
22
0
6
Order By: Relevance
“…The vigorous gasification reactions occurred in the first 30 min, the conversions of ER were 0.195 and 0.75, respectively. This setting was similar to other researchers [21,43]. Figure 4 shows that the volume fraction of gas components changes over oxygen concentration at 650 °C.…”
Section: Effects Of Temperature and Oxygen Concentrationsupporting
confidence: 88%
See 1 more Smart Citation
“…The vigorous gasification reactions occurred in the first 30 min, the conversions of ER were 0.195 and 0.75, respectively. This setting was similar to other researchers [21,43]. Figure 4 shows that the volume fraction of gas components changes over oxygen concentration at 650 °C.…”
Section: Effects Of Temperature and Oxygen Concentrationsupporting
confidence: 88%
“…The vigorous gasification reactions occurred in the first 30 min, the conversions of ER were 0.195 and 0.75, respectively. This setting was similar to other researchers [21,43]. Figure 4 shows that the volume fraction of gas components changes over oxygen concentration at 650 • C. It is clear to see that the combustible components CO, CH 4 , and H 2 show a similar trend, these gases were consumed by excessive oxidation due to more oxygen content, while the trend of CO 2 is the opposite.…”
Section: Effects Of Temperature and Oxygen Concentrationsupporting
confidence: 87%
“…The authors of the investigation [31] have estimated close results that 312 kg/h of MSW are required to produce 107 kg/h of RDF, assuming that 50 % of total MSW are recyclables (ceramics, metals, plastics, glasses, etc. ), water flow in the separated MSW total flow is about 43 kg/h; actcording to real (actual) operation of MSW handling, there were considerable material losses in the milling (3 %) and briquetting (2 %) operations [31]. Table 3 shows a potential of about 1,213 kt/a of MSW which could be treated for RDF production.…”
Section: Estimation Of Potential Benefits Of Implementation Of Co-mentioning
confidence: 97%
“…Gasification is used to convert solid materials such as coal, coke, biomass and solid waste into a gas, with average composition 15-30% CO, 12-40% H, and 4.5-9% CH 4 . The lower heating value (LHV) of syngas is between 4 and 13 MJ/Nm 3 , depending on the oxidizing agent used in gasification, operating conditions, among other factors [34]. From the syngas gas produced, different chemical intermediate products can be obtained, with different industrial uses.…”
Section: Gasificationmentioning
confidence: 99%