2007
DOI: 10.1016/j.ijhydene.2006.08.038
|View full text |Cite
|
Sign up to set email alerts
|

Fireside and steamside corrosion of alloys for USC plants

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

2
30
0

Year Published

2010
2010
2024
2024

Publication Types

Select...
8
1

Relationship

0
9

Authors

Journals

citations
Cited by 74 publications
(32 citation statements)
references
References 3 publications
2
30
0
Order By: Relevance
“…During that stage the process follows the linear Fig. 12 Metal loss of the analysed T23 and T92 after 1000 h exposure at 700 and 750°C dependence which is in agreement with Natesan and Park [25]. After longer time when the protective scale brakes down and the growth of magnetite is possible the rate dependence changes to parabolic; the oxidation rate remains parabolic as long as the developed scale is able to maintain adherence [26].…”
Section: Discussionsupporting
confidence: 84%
“…During that stage the process follows the linear Fig. 12 Metal loss of the analysed T23 and T92 after 1000 h exposure at 700 and 750°C dependence which is in agreement with Natesan and Park [25]. After longer time when the protective scale brakes down and the growth of magnetite is possible the rate dependence changes to parabolic; the oxidation rate remains parabolic as long as the developed scale is able to maintain adherence [26].…”
Section: Discussionsupporting
confidence: 84%
“…Higher efficiency electricity production can be achieved by using steam systems with higher temperatures and pressures to generate electricity. Increases in steam temperatures (up to $700°C) and pressures would increase the overall efficiency of electricity generation up to $50% [3].…”
Section: Introductionmentioning
confidence: 99%
“…The maximum in the curve was first determined using base conditions of the SCM C. This temperature is higher than that found by Reid [15] and Syed [2,57] and just slightly less than that found by Natasan [19]. Tests would need to be conducted at 725 o C to confirm this.…”
Section: Temperature Effectmentioning
confidence: 95%
“…[19] Alkali iron trisulfates are the most probable cause of liquid phase corrosion, because their melting points are in the range of superheater metal temperatures, they have been found in the areas where corrosion has occurred, and they are highly reactive materials. The melting points of some alkali trisulfates are shown in Table 7.…”
Section: Alkali Iron Trisulfatesmentioning
confidence: 99%