Integrated Gasification Combined Cycle (IGCC) Technologies 2017
DOI: 10.1016/b978-0-08-100167-7.00028-7
|View full text |Cite
|
Sign up to set email alerts
|

The gas and steam turbines and combined cycle in IGCC systems

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
11
0
1

Year Published

2021
2021
2024
2024

Publication Types

Select...
9

Relationship

0
9

Authors

Journals

citations
Cited by 17 publications
(12 citation statements)
references
References 71 publications
0
11
0
1
Order By: Relevance
“…The AFT of Barapukurian coal was measured to be higher than 1560°C under reducing atmosphere, as shown in Table 2. The AFT depends on the concentration of mineral matter present in the ash [21]. The higher AFT of Barapukurian coal is potentially due to the higher concentration of Al2O3 with a very high melting temperature [22].…”
Section: Sample Characterisationmentioning
confidence: 99%
“…The AFT of Barapukurian coal was measured to be higher than 1560°C under reducing atmosphere, as shown in Table 2. The AFT depends on the concentration of mineral matter present in the ash [21]. The higher AFT of Barapukurian coal is potentially due to the higher concentration of Al2O3 with a very high melting temperature [22].…”
Section: Sample Characterisationmentioning
confidence: 99%
“…This is due to the fact that H 2 O exhibits a stronger decarbonization ability than CO 2 , both thermodynamically and kinetically. 47 The CO 2 hydrogenation and H 2 O decarbonization processes are similar to those of CO 2 decarbonization without any additional H 2 consumption, as shown in Figure 3f. Coke, as the byproduct of C 3 H 8 dehydrogenation, participates in the decarbonization reaction to produce CO, which is also equivalent to the reforming reaction of CO 2 and C 3 H 8 , where coke serves as a bridge between CO 2 and C 3 H 8 .…”
Section: Resultsmentioning
confidence: 58%
“…Minimum quality of working fluid (x T,min ) during expansion is verified dividing the turbine in ten small-stages and calculating the quality in each small-stage. The small-stages have constant polytropic efficiency (η T, poly ) and pressure ratio (pr T,ss ) as presented in Equation ( 5) [46]. Turbine reheat factor (RH T ) measures the inefficiency of the complete expansion [46] and it is calculated using Equation ( 6) in which ∆h ss,ise is the isentropic small-stage enthalpy difference.…”
Section: Thermodynamic Modelmentioning
confidence: 99%
“…The small-stages have constant polytropic efficiency (η T, poly ) and pressure ratio (pr T,ss ) as presented in Equation ( 5) [46]. Turbine reheat factor (RH T ) measures the inefficiency of the complete expansion [46] and it is calculated using Equation ( 6) in which ∆h ss,ise is the isentropic small-stage enthalpy difference.…”
Section: Thermodynamic Modelmentioning
confidence: 99%