2010
DOI: 10.1016/j.ijggc.2009.09.017
|View full text |Cite
|
Sign up to set email alerts
|

Modeling CO2 capture with aqueous monoethanolamine

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
58
0
1

Year Published

2011
2011
2023
2023

Publication Types

Select...
8

Relationship

1
7

Authors

Journals

citations
Cited by 97 publications
(59 citation statements)
references
References 5 publications
0
58
0
1
Order By: Relevance
“…Therefore the total equivalent work or lost production of electricity is given by: [13][14][15]30]. More recent estimates use 35 wt% MEA with advanced stripper configurations to get heat duties as low as 2.9 MJ/kg [16][17][18]. The values for the KS-1 solvent by MHI have decreased from an early value of 3.3 [19] to a minimum value of 2.6 MJ/kg with an advanced stripper configuration [20,21].…”
Section: Process Flowsheetmentioning
confidence: 99%
“…Therefore the total equivalent work or lost production of electricity is given by: [13][14][15]30]. More recent estimates use 35 wt% MEA with advanced stripper configurations to get heat duties as low as 2.9 MJ/kg [16][17][18]. The values for the KS-1 solvent by MHI have decreased from an early value of 3.3 [19] to a minimum value of 2.6 MJ/kg with an advanced stripper configuration [20,21].…”
Section: Process Flowsheetmentioning
confidence: 99%
“…Effects of pressure and molar ratio of MEA to CO 2 As shown in Fig. 5, compared with 0.1 MPa pressure, when CO 2 absorption operated under 1 MPa pressure , better results of CO 2 conversio n were obtained and its tendencies along the gas flow rate were much more stable. For example, CO 2 conversion almost kept constant at 99.2% under 1 MPa pressure at the molar ratio of 3.72.…”
Section: Effects Of Temperaturementioning
confidence: 94%
“…Global warming and climate change have motivated extensive researches towards developing improved and more efficient technologie s for CO 2 capture from large point sources, such as natural gas, coal based power plant, floating liquefied natural gas plant (FLNG) and refinery off-gases. At present, the most widely utilized technique for CO 2 removal is CO 2 absorption by alkanolamine-base d chemical solvents.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…, 흡수제 압축 및 재순환 공정(Lean Vapor Compression Configuration) [5], 이중 탈거탑 장 치(Matrix Stripper) [6], 흡수제 분할 공정(Split-Flow Configuration) [7][8][9][10], 다단 플래시 탈착 공정(Three-stage flash for stripping) [11], 발전-포 집 연계 공정(Integration of power plant and amine scrubbing) [10,[12][13][14] …”
Section: 서 론unclassified