2017
DOI: 10.1016/j.applthermaleng.2016.08.178
|View full text |Cite
|
Sign up to set email alerts
|

Water extraction from high moisture lignite by means of efficient integration of waste heat and water recovery technologies with flue gas pre-drying system

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
2

Citation Types

0
7
0

Year Published

2017
2017
2023
2023

Publication Types

Select...
6
2

Relationship

1
7

Authors

Journals

citations
Cited by 46 publications
(7 citation statements)
references
References 46 publications
0
7
0
Order By: Relevance
“…c: Cost is quoted from Moaseri [29]. d: The parameters are based on [15].e: The parameters are based on [26,30].…”
Section: Estimation Of the Total Investment Costmentioning
confidence: 99%
See 1 more Smart Citation
“…c: Cost is quoted from Moaseri [29]. d: The parameters are based on [15].e: The parameters are based on [26,30].…”
Section: Estimation Of the Total Investment Costmentioning
confidence: 99%
“…Except for those traditional measures to improve the performance of the steam cycle design [8,9], e.g., employing more feedwater preheaters or reheaters [8,[10][11][12] and applying optimal steam cycle design [8,13,14], another effective way, which has been a hot topic in recent years [15,16], is the indepth utilization of low-temperature waste heat from the exhausted flue gas. To achieve this goal, mostly low-temperature economizers (LTE) are configured after or parallel to the air preheater to recover the waste heat from the flue gas to heat up a part of the condensate water [17,18].…”
Section: Introductionmentioning
confidence: 99%
“…Normally, the amount of desulfurization wastewater produced is 15 to 20 kg/(MW•h). Accordingly, the flow rate of desulfurization wastewater produced by 600 MW units was estimated around 10 m 3 /h [2,3]. Although it is much lower than that in seawater desalination plants, the desulfurization wastewater is generally featured by high content of suspended solids, COD (chemical oxygen demand), fluoride and heavy metals such as As, Hg, Pb [4].…”
Section: Introductionmentioning
confidence: 99%
“…c: Cost is quoted from Moaseri [33]. d : The parameters are based on [19]. e : The parameters are based on [22,30].…”
Section: Estimation Of the Total Investment Costmentioning
confidence: 99%
“…In addition to the traditional measures used to improve the performance of the steam cycle design [8][9][10], e.g., employing more feedwater preheaters or reheaters [11][12][13][14][15][16] and applying optimal steam cycle design [11,17,18], another effective way which has been widely discussed in recent years [19,20], is the in-depth utilization of low-temperature waste heat from the exhausted flue gas. To achieve this, low-temperature economizers (LTEs) are usually configured after or parallel to the air preheater to recover the waste heat from the flue gas to heat up a part of the condensate water [21,22].…”
Section: Introductionmentioning
confidence: 99%